| HS Code | 745162 |
| Product Name | N-Propanol for Printing Inks |
| Chemical Formula | CH3CH2CH2OH |
| Cas Number | 71-23-8 |
| Molecular Weight | 60.10 g/mol |
| Appearance | Clear, colorless liquid |
| Assay Purity | ≥ 99.5% |
| Boiling Point | 97.2 °C |
| Flash Point | 22 °C (closed cup) |
| Vapor Pressure | 20 mmHg at 20 °C |
| Evaporation Rate | 1.0 (n-butyl acetate = 1) |
| Viscosity | 2.26 mPa·s at 20 °C |
| Density | 0.803 g/cm³ at 20 °C |
| Refractive Index | 1.384 at 20 °C |
| Solubility In Water | Miscible |
| Hygroscopicity | Slightly hygroscopic |
As an accredited N-Propanol for Printing Inks factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | N-Propanol for Printing Inks: supplied in 160 kg drums or 800 kg IBC totes, with secure lids and labels. |
| Container Loading (20′ FCL) | N-Propanol for printing inks is loaded as drummed, palletized cargo in a 20′ FCL, secured and segregated for safe transport. |
| Shipping | Shipping: N-Propanol for Printing Inks is a flammable liquid (UN1274, Class 3). Transport in properly sealed, labeled drums or bulk tankers, segregated from oxidizers and ignition sources. Ensure compliant hazardous-material documentation, secure loading, and adequate ventilation. Follow all applicable regulations for road, rail, sea, or air freight. |
| Storage | Store N-Propanol for printing inks in a cool, well-ventilated area away from heat, sparks, and open flames. Keep containers tightly sealed and clearly labeled. Use approved materials like stainless steel or glass. Isolate from oxidizing agents and incompatible chemicals. Ensure proper grounding to prevent static discharge, and follow local flammable liquid storage regulations. |
| Shelf Life | N-Propanol for Printing Inks has a shelf life of approximately two years when stored properly in original sealed containers. |
In solvent-based flexographic surface printing for monolayer BOPP and PE pouch structures, n-propanol (CAS 71-23-8) is introduced as a medium-volatility tail solvent in nitrocellulose/polyurethane letdown systems. The solvent is selected because its boiling point of 97.2 °C and closed-cup flash point of 22 °C position it between ethyl acetate and propyl acetate in the evaporation hierarchy, preventing premature cell dry-up on ceramic anilox rolls without extending oven residence time beyond the solvent extraction capacity of a 6-zone central impression press. In a starting formulation for 300 m/min polyethylene surface work, n-propanol addition is maintained at 8–15 wt% of final ink mass; below 8 wt% the ink exhibits dot skips and pinholing in 60–65 °C inter-deck drying, while above 20 wt% solvent-sensitive photopolymer sleeve swell becomes measurable as shoulder edge rounding under 175 LPI imaging targets. The downstream production process includes high-shear predispersion of nitrocellulose and polyurethane in a Cowles dissolver at 3000–4500 rpm, followed by letdown at 20–30 °C to 22–28 s Zahn cup #2 at 25 °C, and application through a 500–800 LPI ceramic anilox with a volume of 4.0–7.0 BCM and a chambered doctor blade. Nitrocellulose wetting is completed before n-propanol letdown because reverse addition can create localised high-alcohol zones that precipitate resin solids; letdown temperature is held below 30 °C to limit volatile loss. On press, evaporation of n-propanol from the printed film is governed by inter-deck air speed of 8–15 m/s and web temperature rather than by alcohol content alone. Compliance for food-contact substrate applications is managed under Regulation (EC) No 1935/2004, Article 3, Regulation (EC) No 2023/2006, Annex, and EuPIA GMP for non-direct food contact inks, with residual-solvent control verified by headspace GC against converter specifications rather than a single harmonised n-propanol SML because published data for n-propanol-specific migration in this configuration is limited. Terminal product types include printed BOPP snack-food pouches, PE lidding films, and overwrap films where the ink remains surface-applied or is laminated into adhesive-containing structures.
| Downstream segment | Standard/regulation | Clause or test method | Controlled parameter |
|---|---|---|---|
| Solvent-based flexo food packaging | Regulation (EC) No 1935/2004 | Article 3 | No transfer of constituents in quantities endangering human health |
| Solvent-based flexo food packaging | Regulation (EC) No 2023/2006 | Annex | Good manufacturing practice for food-contact inks |
| Rotogravure lamination inks | ISO 11890-2:2020 | Method | VOC content of solvent-based ink |
| Water-based flexo corrugated inks | ISO 11890-2:2020 | Method | VOC content of water-based ink |
| Continuous inkjet coding | Regulation (EC) No 1272/2008 | H225, H318, H336 | Flammability and health hazard classification |
For reverse-printed PET and aluminium-foil lamination structures destined for confectionery and pharmaceutical blister lidding, n-propanol is added at 4–10 wt% of final ink mass to adjust the evaporation gradient between ethyl acetate and propyl acetate. The production sequence on a rotary gravure line starts with ink adjustment to 15–18 s DIN 4 mm cup at 25 °C, transfer from a diamond-stylus-engraved cylinder with cell depth of 32–45 µm, and printing at 120–300 m/min through 60–90 °C drying hoods. The evaporation hierarchy in the gravure cell is influenced by cylinder temperature and air impingement; n-propanol is retained longer than ethyl acetate in the engraved cell, which allows resin redissolution during brief press stops but increases solvent retention if the printed web is wound before the film temperature drops below 30 °C. Above 12 wt%, retained solvent in the printed layer becomes the critical defect mechanism in solventless lamination, producing peel-strength reduction when tested by ISO 11339:2022 T-peel after 24 h cure; below 4 wt%, gravure cell dry-up during reel splices and register adjustments creates dot skips in 70 L/cm engraving screens. Compliance for VOC content of the ready-to-use ink is determined by ISO 11890-2:2020, and press emissions fall under Directive 2010/75/EU Annex VII where solvent recovery or thermal oxidation is installed; packaging-grade converters commonly specify total retained solvent via headspace GC because no single ISO method covers all lamination structures. Terminal product types are reverse-printed PET/aluminium foil lidding, multi-layer confectionery wrappers, and pharmaceutical blister foils printed on the non-sealing side.
Water-based flexographic inks for corrugated board and kraft paper receive n-propanol at 1.5–3.0 wt% of final ink mass as a co-solvent to reduce dynamic surface tension and shift drying rate after letdown. The pH is first adjusted to 8.8–9.4 with a volatile amine, then viscosity is set to 20–30 s Zahn cup #2 at 25 °C; application proceeds through an anilox volume of 3.0–5.5 BCM on a flexo folder-gluer running at 100–250 boards/min. Above 5.0 wt% n-propanol, styrene-acrylic emulsion stability decreases, observable as filter clogging and persistent foam under high-speed circulation; below 1.0 wt%, the wet film remains on uncoated board too long and creates setoff at stack temperatures above 40 °C. VOC content is determined by ISO 11890-2:2020; food-contact use requires a functional barrier or proof of low migration because published data for n-propanol migration through water-based flexo ink films on recycled board is limited. Terminal product types are recycled corrugated shipping boxes, shelf-ready retail cartons, and paper bags printed at low stack temperatures.
Within continuous inkjet fluids used for date and batch coding on beverage cans, extruded cable sheathing, and pharmaceutical cartons, n-propanol is used as co-solvent at 5–20 wt% of total ink mass in a solvent matrix that may also contain ethanol or methyl ethyl ketone. The downstream operation includes ink circulation through a 36–75 µm nozzle at 0.8–2.5 bar, piezo-driven drop break-off at 60–100 kHz, and gutter recovery of un-printed droplets. N-propanol shifts evaporation so that nozzle dry-up during line stops of 5–10 min is reduced relative to ethanol-only formulations; however, because its kinematic viscosity is higher than ethanol, the ink requires a higher drive voltage to maintain drop placement accuracy within ±0.5 mm at 2 m/s product speed. Production limits are controlled by viscosity and conductivity rather than a single fixed solvent rule, with typical operating viscosity of 2–6 mPa·s at 25 °C. Compliance for flammable solvent handling follows Regulation (EC) No 1272/2008 CLP classification H225, H318, H336 and storage under NFPA 30; when codes are applied to food packaging, EuPIA GMP for non-direct food contact applies and the print must remain on the non-food-contact side or be applied before a functional barrier is created because published data for n-propanol migration through inkjet ink films is limited. Terminal product types include shelf-life date codes on metal cans, batch numbers on PVC cable insulation, and 2D matrix codes on glass pharmaceutical vials.
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n-Propanol (CAS 71-23-8; normal propyl alcohol; 1-propanol) is a linear C3 primary alcohol supplied as a printing-ink solvent for flexographic and gravure dilution where a mid-boiling, water-miscible alcohol is required to dissolve polar resins and control drying. A typical printing-ink grade is specified with a purity of ≥ 99.5 wt%, water content of ≤ 0.10 wt%, acidity as acetic acid of ≤ 0.002 wt%, and non-volatile residue of ≤ 0.001 wt%; these values should be confirmed on the supplier certificate of analysis, as no single industrial grade covers all printer-specific formulations. The substance is classified under EC 1272/2008 as Flam. Liq. 2 (H225), Eye Dam. 1 (H318), and STOT SE 3 (H336), with UN transport code UN 1274, Class 3, Packing Group II.
In ink formulation, n-propanol is used less as a bulk let-down solvent and more as a solvency and viscosity modifier for nitrocellulose and polyamide binders. Its primary hydroxyl group and linear C3 chain provide hydrogen bonding with amide linkages and nitrocellulose hydroxyl sites, which lowers flow time and improves pigment wetting. In high-solids polyamide surface-printing inks, n-propanol is added at 5–15 wt% of the total solvent blend; viscosity is checked on a Zahn #2 cup according to ASTM D4212, with typical press-ready flow times of 22–28 s. The exact amount depends on the pigment load, resin acid number, and cylinder or anilox engravings used on the converting line.
| Property | n-Propanol | Isopropanol | Ethanol | Test method or source |
|---|---|---|---|---|
| Molecular weight | 60.10 g/mol | 60.10 g/mol | 46.07 g/mol | calculated |
| Boiling point at 101.325 kPa | 97.2 °C | 82.5 °C | 78.3 °C | ASTM D1078 |
| Flash point, closed cup | 22 °C | 12 °C | 13 °C | ASTM D56 |
| Vapour pressure at 20 °C | 2.0 kPa | 4.4 kPa | 5.8 kPa | reported static values |
| Density at 20 °C | 0.803 g/cm³ | 0.785 g/cm³ | 0.789 g/cm³ | ASTM D4052 |
| Surface tension at 20 °C | 23.8 mN/m | 21.7 mN/m | 22.1 mN/m | du Noüy ring |
| Explosive limits in air | 2.1–13.5 vol% | 2.0–12.7 vol% | 3.3–19.0 vol% | ASTM E681 |
On central-impression flexographic presses operating at line speeds above 200 m/min, n-propanol is introduced at the viscosity control station to reduce dry-in at the anilox surface and to extend open time on the plate. The solvent balance is adjusted after monitoring flow time and print quality; if the press-ready ink falls below 22 s on a Zahn #2 cup, misting can occur at the nip, while values above 28 s may produce pinholing or cobwebs on fine reverse-print work. A 2–5 wt% n-propanol addition frequently restores flow without the faster evaporation associated with ethanol or isopropanol. On paper and board substrates, n-propanol also reduces water absorption into the stock, which helps control fibre swell and plate plugging on uncoated grades.
In gravure surface printing, the same solvent is used as a medium-boiling retarder for the last colour station. Engraved cylinders with cell depths of 30–40 µm and high line rulings can dry in the cells if the diluent is too fast; n-propanol prolongs cell release and allows clean tonal transfer. The addition is typically made at the ink sump or through an automatic diluent feed and is cross-checked by measuring the ink tray solids or viscosity. At higher addition levels, the drying tunnel must be operated with sufficient air velocity to reduce retained solvent before the web enters the rewind.
The primary operational difference is boiling point and solvent-release rate. n-Propanol boils at 97.2 °C at 101.325 kPa, approximately 15 °C higher than isopropanol, which extends open time but increases the risk of retained solvent in fast lamination lines. The solvency difference is also measurable: n-propanol has a stronger swelling effect on alcohol-soluble polyamide resins, producing a greater viscosity reduction for the same weight fraction in high-solids systems. In nitrocellulose-based inks, n-propanol improves flow and reduces matte surface roughness, but at levels above 10–15 wt% it can retain solvent sufficiently to soften blocking on collation reels unless rewinding tension is reduced and drying conditions are increased.
Compared with ethanol, n-propanol has lower vapour pressure and lower evaporation rate, making it useful where print cylinder or plate dry-in occurs. Ethanol is more hygroscopic and can raise equilibrium water content faster in humid pressrooms; n-propanol is not a moisture barrier, but its lower evaporation rate reduces evaporative cooling and condensation of water onto the ink surface. In water-reducible systems, n-propanol functions as a coupling solvent and lower-surface-tension component; its surface tension of 23.8 mN/m is significantly below that of water, aiding wetting on low-energy films.
Compared with n-propyl acetate, the defining difference is the absence of an ester group and the presence of the hydroxyl group. n-Propyl acetate has a boiling point near 101.6 °C but a lower flash point of 13 °C and no active hydrogen. Replacing n-propanol with n-propyl acetate raises viscosity and can cause resin incompatibility in polyamide-rich formulations; replacing n-propyl acetate with n-propanol may increase wetting and resin solubility but can reduce solvent-release speed and increase moisture uptake. Compared with 1-methoxy-2-propanol, n-propanol evaporates faster, is less hydrophobic, and has a lower molecular weight; the glycol ether is selected when stronger retardation and higher solvency for polyester or acrylic resins are required.
Resin solvency is commonly evaluated by turbidity titration or constant-temperature solubility testing. n-Propanol gives a wider clear region with alcohol-soluble polyamide than isopropanol when the resin acid number is between 5 and 20 mg KOH/g; the ester/alcohol ratio in the diluent can then be shifted to a higher ester content without precipitation. This permits formulators to reduce retained-alcohol content while preserving nitrocellulose compatibility. The same interaction is observed in dispersion work: pigment concentrates based on phthalocyanine blue or carbon black can maintain longer recirculation stability when n-propanol replaces isopropanol on an equal weight basis.
At relative humidity above 65%, alcohol-based inks absorb atmospheric moisture; because water is not a true solvent for nitrocellulose/polyamide formulations, the viscosity can drift upward or phase separation can appear. n-Propanol partially buffers this effect through water miscibility, but it does not eliminate the hygroscopic response. Press trials on a CI flexo line using an 8-colour configuration and a 1.2 m web width indicated that replacing 3% of the ethanol with n-propanol reduced viscosity drift over a 4 h run by maintaining a more uniform solvent balance, although published data for this specific configuration is limited and the result depends on ink design and air handling.
n-Propanol is generally unsuitable as a diluent in the isocyanate-reactive portion of two-component PU lamination inks because the primary hydroxyl group consumes free isocyanate and reduces crosslink density. The resulting workable pot life can decrease from several hours to under 60 min in warm pressroom conditions, and final peel strength may fall below the required structural adhesion level for high-barrier laminates. If n-propanol is used in the pigment dispersion or mill-base, the solvent should be evaporated before the hardener is added, or the formulation must be rebalanced to maintain the target NCO:OH ratio. For standard retort and boil-in-bag structures, ester and ketone diluents such as ethyl acetate and methyl ethyl ketone are preferred; n-propanol remains viable only in one-component NC/PA surface inks or where the converter has validated the specific laminate construction.
The same reactivity constraint applies to radiation-curable ink formulations that contain free isocyanate adhesion promoters or urethane acrylates with residual NCO. n-Propanol competes for the isocyanate and can interfere with the curing mechanism; addition is not recommended unless the ink supplier has verified chemical compatibility and real-time viscosity stability.
| Parameter | Standard or code | Typical value or requirement |
|---|---|---|
| Flash point | ASTM D56 | 22 °C closed cup |
| Density at 20 °C | ASTM D4052 | 0.803 g/cm³ |
| Dip-cup flow time | ASTM D4212 | 22–28 s Zahn #2 |
| VOC content | ISO 11890-2 / ASTM D2369 | Measured in g/L; limit depends on local air quality regulation |
| Residual solvent in printed films | HS-GC method aligned with ISO 11890-2 | Below converter-specific limit; often cited below 5 mg/m² in high-barrier laminates |
| EU CLP classification | EC 1272/2008 | Flam. Liq. 2; Eye Dam. 1; STOT SE 3 |
| Transport | UN 1274 | Class 3, Packing Group II |
| REACH registration | EC 1907/2006 | Registered as full substance; check current status |
Storage tanks and transfer lines for n-propanol should be earthed and bonded because the solvent has low electrical conductivity and can accumulate static charge during pumping. The flash point of 22 °C closed cup and lower explosive limit of 2.1 vol% require ventilation that prevents vapour concentrations above 25% of the lower explosive limit. Seal and gasket compatibility should be selected from chemical resistance data for PTFE, EPDM, or high-grade nitrile; natural rubber and some flexible PVC tubing are unsuitable due to swelling and plasticiser extraction. Drum pumps should be fabricated from stainless steel or conductive polypropylene with explosion-proof motors rated for flammable atmospheres.
In plants that operate solvent-recovery distillation, n-propanol can be recovered together with ethanol and isopropanol from the dryer exhaust. Separation requires a distillation column with sufficient theoretical plates because the boiling-point difference between n-propanol and isopropanol is only 15 °C, and the n-propanol/water azeotrope at approximately 71.7 wt% n-propanol boils at 87.7 °C. The recovered stream must be monitored for water content and acidity before reuse; high water levels shift ink viscosity and can interfere with nitrocellulose solubility.
Waterborne flexo inks occasionally use n-propanol at 2–5 wt% to improve rewetting of anilox rolls and to reduce surface defects on film substrates. The solvent is fully miscible with water and can be pre-blended into amine-neutralized acrylic systems when pH is maintained between 8.2 and 9.0. This addition raises VOC content and must be accounted for in the formulation’s regulatory VOC calculation; it is typically limited to the minimum required to maintain clean anilox cell release and stable film formation.
For solvent-borne ink manufacturers, n-propanol often replaces a portion of isopropanol in polyamide surface-printing series when the converter reports excessive plate dry-in or when the resin supplier specifies a slower alcohol. The substitution is not straightforward: because n-propanol reduces viscosity more efficiently, the formulator may need to reduce the solvent level or increase the resin concentration to maintain the same flow time and film build. Conversely, replacing ethanol with n-propanol can improve wetting but can also increase retained solvent; therefore the final formulation is normally qualified by headspace GC and blocking tests rather than by blending rule alone.
In food-contact printing, the use of n-propanol must follow migration assessment principles in the EuPIA Good Manufacturing Practice and, where applicable, the Swiss Ordinance SR 817.023.21. The low odour threshold of n-propanol can make residual amounts perceptible before toxicological limits are reached, so sensory panels are sometimes used alongside HS-GC analysis. This does not alter the legal status; it is an operational control for brand owners.
n-Propanol also appears in cleaning blends for ink trays, plates, and anilox rolls when the same resin system is used; its aggressiveness toward dried polyamide and NC films falls between ethanol and glycol ethers. Such blends are usually non-specification and are governed by equipment manufacturer compatibility statements.