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Polyol

Polyols are a class of organic compounds that contain multiple hydroxyl (-OH) groups.
They are widely used in a variety of applications, including the production of plastics, adhesives, and personal care products.
Polyols can be derived from natural sources, such as plant oils and sugars, or synthesized from petrochemical feedstocks.
Their unique properties, such as low toxicity, high viscosity, and water solubility, make them valuable in many industries.
Polyol research focuses on optimizing synthesis methods, improving product quality, and developing new applications for these versatile compounds.
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Most cited protocols related to «Polyol»

All molecular mechanics calculations were performed with the CHARMM program.20 ,25 The all-atom additive CHARMM force field uses the energy potential U(r) given in Equation 1. U(r)=ΣbondsKb(bb0)2+ΣanglesKθ(θθ0)2+ΣUreyBradleyKUB(SS0)2+ΣdihedralsKχ(1+cos(nχσ))+ΣimpropersKimp(φφ0)+Σnonbonedεij[(Rmin,ijrij)122(Rmin,ijrij)6]+qiqjrij In Equation 1, Kb, Kθ, KUB, Kχ and Kimp are bond, valence angle, Urey-Bradley, dihedral angle, and improper dihedral angle force constants, respectively, while b, θ, S, χ and φ are the bond distance, valence angle, Urey-Bradley 1,3-distance, dihedral angle and improper dihedral angle, respectively, where the subscript zero represents the equilibrium value. In the dihedral potential energy term, n is the multiplicity and σ is the phase angle as in a Fourier series. The nonbonded interaction energy between atoms i and j is separated into two terms, the Lennard-Jones (LJ) 6-12 term and the Coulomb term. For the nonbonded terms, εij is the LJ well depth, Rmin,ij is the distance at the LJ energy minimum, qi and qj are the partial atomic charges, and rij is the distance between atoms i and j. For the LJ parameters, the Lorentz-Berthelot combining rules are applied.26
Hydrogen bonding water-solute pair interaction energies and distances were calculated using the standard additive CHARMM force field protocol, so as to maintain compatibility with existing CHARMM biomolecular force fields.19 ,21 (link) Solute geometries were obtained from optimization at the MP2/6-31G(d) level of the conformation in the respective crystals obtained from the Cambridge Structural Database.23 Using the optimized geometry of the monomer, water-monomer pairs were constructed, with the water internal geometry identical to that of the TIP3P water model.27 Examples of these pair interactions are shown in Figure 2 where the water molecule is interacting with the terminal hydroxyl of allitol. In pairs 1, 2, 3 and 4 the hydroxyl oxygen is the hydrogen bond donor and in 5 and 6 the hydroxyl hydrogen is the hydrogen bond acceptor. For pairs 1, 2, 3 and 4 the hydrogen of the water molecule is directed at the COH bisector. In pairs 1 and 2 the water molecule lies in the COH plane whereas in pairs 3 and 4 the water molecule lies at a 120 degrees angle to the COH plane. Pairs 5 and 6 are different because the water molecule in these interaction pairs acts as the hydrogen bond acceptor; therefore, the COH hydroxyl is directed along the water HOH bisector. For pair 5, the HOH plane of the water is at a 90-degree angle to the COH plane, and for pair 6 the HOH and COH atoms are coplanar.
Reference data for comparison of molecular mechanics (MM) interaction energies and distances were generated by geometry optimization of the interaction distances at the QM HF/6-31G(d) level for each of the water-solute pairs above, with all other degrees of freedom constrained. The QM data cannot be targeted directly, but are instead empirically scaled to account for the fact that the MM force field needs to be able to account for many-body effects in the condensed phase. The CHARMM additive force field empirical scaling rules are well-established15 ,28 and are such that the MM target distance is the RQM − 0.2 Å and the MM target pair interaction energy (denoted “EQM”) is given by the expression 1.16*(EQM,pairEQM,soluteEQM,water). The energy-scaling factor of 1.16 and the offset of the QM distance by 0.2 Å account for limitations in the potential energy function and in the QM level of theory, and these empirical corrections lead to good agreement with condensed phase properties, as shown in previous work.20 ,21 (link)
All of the C-C-C-C, C-C-C-O, O-C-C-O and C-C-O-H dihedral parameters are fit to relaxed QM potential energy scans. The Gaussian03 package29 is used to optimize geometries at the MP2/6-31G(d) level of theory followed by single point calculations performed at the RIMP2/cc-pVTZ level with the QCHEM program.30 (link) This level of theory has previously been shown to be sufficiently accurate for a number of systems including carbohydrates.22 (link),31 (link) The target dihedral is scanned at 15° intervals from −180 to 165°, with the exception of inositol, which is scanned from 15 to 135° due to the constrained nature of the ring. The dihedral parameters are then fit to the QM dihedral scans using an automated Monte Carlo simulated annealing (MCSA) method.24 (link) In the MCSA method the selected dihedral parameters are fit simultaneously to minimize the root mean squared error (RMSE), RMSE=Σiwi(EiQMEiMM+c)2Σiwi, where EiQM and EiMM are the QM and MM energies of conformation i, wi is a weighting factor for conformation i and c is a constant that aligns the QM and MM data to minimize the RMSE. All of the six-carbon (n=6) alditols are used in the fitting procedure (Figure 1) and all of the five-carbon (n=5) and four-carbon (n=4) alditols are used as the test set for the parameter validation. With inositol, the C-C-C-O, O-C-C-O and C-C-O-H dihedrals are transferred from the hexopyranose parameters and only the C-C-C-C is fit (independently from the n=6 alditols). For the dihedral parameters in the aldehyde and ketone groups in the linear carbohydrates D-allose and D-psicose (Figure 1), only the torsions containing non-hydrogen atoms and including the carbonyl atoms are parametrized and the other torsional parameters are transferred from the n=6 alditols.
Parameter optimization and validation of the parameters is performed via a number of condensed phase MD simulations. A cubic box containing TIP3P water molecules27 ,32 with periodic boundary conditions is used for all aqueous simulations. Particle Mesh Ewald (PME)33 with a 12 Å real space cutoff is used to treat the long-range Coulomb interactions and a force-switched smoothing function34 with a range of 10-12 Å is used for the Lennard-Jones interactions, with a long-range correction applied beyond the truncation distance.26 The SHAKE algorithm35 is used to constrain all hydrogen atom bonds to their equilibrium lengths and to maintain rigid water geometries. For the constant pressure – constant temperature (NPT) simulations the Nosé-Hoover thermostat36 ,37 (link) is used to maintain the temperature and the Langevin piston barostat38 is used to maintain the pressure. A leapfrog integrator39 is used with a 1 fs timestep for all of the simulations.
Pure solvent simulations are performed with a periodic box of 125 solvent molecules. The box of solvent molecules is minimized and then equilibrated for 50 ps followed by five production runs performed for 1 ns. The heat of vaporization ΔHvap is calculated from the pure solvent simulation using the relation ΔHvap=UmonomerUboxN+RT Here, 〈Umonomer is the average potential energy of the monomers calculated from five individual gas-phase simulations of all 125 molecules, with each simulation run for 500 ps. The 〈Ubox term is the average potential energy of the periodic box. N is the number of molecules in the box, R is the universal gas constant for an ideal gas and T is the temperature.
The free energy of aqueous solvation ΔGsol is calculated from the difference in free energy of a molecule in aqueous solution compared to that in the gas phase. ΔGsol is calculated from the sum of nonpolar ΔGnp and electrostatic ΔGelec free energies40 : ΔGsol=ΔGnp+ΔGelec. ΔGnp is the sum of the repulsive and dispersive contribution, which are calculated using the Weeks, Chandler, Anderson decomposition of the LJ potential.41 The repulsion term in the LJ potential is treated using a soft-core potential.42 In the aqueous phase, free energy calculations are performed using 1 molecule centered in a water box of 250 TIP3P water molecules. The aqueous system at each window is equilibrated for 50 ps and then simulated for 200 ps in the NPT ensemble. In the gas phase, Langevin dynamics are used with an infinite non-bond cutoff.26 ,43 Since the gas phase energies converge much more quickly, the gas phase system is equilibrated for 10 ps and the production run is simulated for 100 ps. The simulations are performed at a temperature of 298K and a pressure of 1 atm, which is consistent with experiment. The free energy calculations are analyzed using thermodynamic integration44 and the weighted-histogram analysis method45 (WHAM). Additional details for calculating the free energy have been described previously.40 ,46 Unlike all other condensed phase simulations in the present work, due to software limitations, the long-range pressure correction is not part of the MD protocol for the free energy simulations. Thus, the long-range contribution (LRC) from the LJ potential to the free energy of solvation is calculated as the difference in LJ energy of the aqueous system with a nonbond cutoff of 12 Å and a nonbond cutoff of 30 Å. The LRC is calculated from a 5 ps NPT simulation trajectory of the molecules in solution using coordinates saved every 100 fs and averaged over all values.
From the pure solvent simulation trajectories, the self-diffusion coefficient Dsim incorporates a system-size dependent finite-size correction developed by Yeh and Hummer47 : Dsim=DPBC+kBTζ6πηL. In Equation 5, DPBC is the diffusion coefficient calculated from a simulation with periodic boundary conditions to which the correction term is added. ζ is a constant of 2.837297, kB is the Boltzmann constant, T is the temperature, η is the viscosity and L is the length of the cubic simulation box. DPBC is calculated from the slope of the mean square displacement of the C1 atom of all solute molecules in the simulation box versus time.26 For diffusion coefficients of polyols in aqueous solutions of TIP3P water, Equation 5 is further modified to take into account the low viscosity of TIP3P water relative to experiment: Dsim=DPBC+kBTζ6πηL0.375 η=ηTIP3P(1+2.5ϕ) Here, the scaling factor of 0.375 is applied to correct for the underestimation of the viscosity of water by the TIP3P model. The scaling factor is calculated from ηTIP3P /ηw where ηTIP3P = 0.35 cP and ηw = 0.93 cP, the experimental viscosity of water. Equation 6b is the viscosity of a solution with the presence of a solute estimated by the Einstein formula,48 where ηTIP3P is the viscosity of TIP3P (0.35 cP) and ϕ is the volume fraction of the solute. The method for calculating the simulation diffusion coefficient for a polyol-water mixture is similar to that previously used for a system of polyethylene oxide and polyethylene glycol.49 (link)
Complete crystal unit cells, obtained from the Cambridge Structural Database,23 are used as starting structures for crystal simulations, with periodic boundary conditions applied in accordance with the length and angle parameters of the respective crystals. Each crystal system is minimized initially to remove bad contacts and is then equilibrated for 100 ps. After equilibration, the simulation is run for 2 ns. For all of the polyol crystals, the reference temperature is set to room temperature 298K, the temperature at which the crystals were obtained, and constant pressure is maintained at 1 atm by allowing independent variation in the crystal cell length parameters.
For the aqueous phase MD simulations, a box containing 1100 waters and the number of solute molecules based on the experimental concentration is set up and then minimized using harmonic restraints with a force constant of 1*(particle mass)*kcal*mol−1*Å−2*amu−1 on only the solute molecules. The system is equilibrated for 500 ps and then the equilibrated conformation is used as the starting conformations for five different unrestrained 1ns runs, using different initial velocities for each of the runs to achieve improved statistics. The reference pressure of the glucitol and mannitol systems is 1 atm, and the reference pressure of the galacitol, xylitol, erythritol, ribitol, glycerol and myoinositol system is 3.5 atm, in accordance with the experimental conditions. The density of each system is calculated using the following equations: ρ=NV N=(Nwater+Nsolute)MWNAvogadro where 〈V〉 is the average volume calculated from all five runs. Nwater , Nsolute and NAvogadro are the number of water molecules, the number of polyol solute molecules and Avogadro's number respectively. 〈MW〉 is the average molecular weight of the system. Equation 7a is also used to calculate the density for neat liquids; however, in this case N is simply the number of molecules in the periodic box.
The J coupling constants for glucitol and mannitol are also calculated from the aqueous simulations described above. However, the coupling constants for arabitol, ribitol and xylitol are calculated from aqueous phase simulations at 1 atm and a molality of 0.5 mol*kg−1 using the same protocol for the aqueous simulations. The dihedral value for the proton-proton coupling is calculated every 1 ps for each of the production runs. Moreover, the dihedral value is calculated for each of the solute molecules in the respective systems; therefore, depending on the concentration of the simulation the amount of torsional data differs. The J coupling is then calculated from the dihedral values for each snapshot using the generalized Karplus equation 50 J=0.8cosϕ+10.2cos2ϕ, where ϕ is the H-X-X-H dihedral angle. Manipulation of the Karplus equation given in Equation 8 allows the fraction of trans conformers to be calculated:50 Ftrans=(Jobs3.0)(9.43.0) In Equation 9, Jobs is the observed coupling constant.
Publication 2009
The four TOFA-based bio-polyols were used for rigid PU foam development. The developed rigid PU foam formulations are depicted in Table 2. Bio-polyol with lower functionality based on tall oil (TO) esterification with TEOA (ester polyol TO_TEOA) previously developed by our research group was also used in PU foam formulations [61 (link),62 (link)]. Varied mass ratios of the TO_TEOA with OHval of 334 mg KOH/g, water content of 0.45 wt.%, viscosity of 280 mPa⋅s at 25 °C, fn = 2.4 and Mn = 391, and newly synthesized bio-polyols were used to find optimal rigid PU foam formulations. Previous experience showed that it is necessary to add polyether type polyol into rigid PU foam formulations to enhance the bio-polyol miscibility with water. Thus, a small amount of glycerol was used. Glycerol can also be derived from renewable feedstock and thus would form the third bio-based crosslink polyol in PU formulations [63 (link)]. A combination of two blowing agents, a chemical blowing agent (distilled water) and a physical blowing agent (c-pentane) was used. The chemical blowing agent content was kept constant at 2 parts by weight (pbw) as its variation would impact the chemical composition of the rigid PU foam polymer matrix. The amount of physical blowing agent was varied between 0–15 pbw and its influence on the apparent density of the developed rigid PU foam was studied. A constant amount of TCPP flame retardant (8 wt.%) of PU foam mass was selected for all developed rigid PU foam formulations. TCPP is commonly used in rigid PU foams that are applied in civil engineering. Lastly, all rigid PU foam formulations had a set isocyanate index of 150. The catalyst package was adjusted for each of the TOFA-based bio-polyol series to ensure good PU foam properties.
Furthermore, sustainable material content, as well as the green carbon content of the developed materials were calculated. The sustainable material content was expressed as the total mass of renewable feedstock in PU formulation divided by the total mass of PU formulation; the value was multiplied by a factor of 100, and result expressed in percent (%). The sustainable material content of each synthesized bio-polyol is depicted in Table 1, whereas tall oil content in TO_TEOA polyol was 60%. The green carbon content was expressed as the total mass of green carbon in renewable feedstock divided by the total amount of carbons in PU formulation; the value was multiplied by a factor of 100 and expressed in percent (%). For bio-polyols, the idealized structure was assumed in the calculation. The green carbon content was slightly higher than sustainable material content because the non-renewable raw materials contain many non-carbon elements, such as nitrogen, phosphorous, and chlorine.
The substances listed in Table 2 (green polyols, catalyst, blowing agent, surfactant, and flame retardant) were used to prepare the polyol component of the rigid PU foams by stirring them for 1 min with a mechanical stirrer at 2000 rpm. Afterwards, the polyol component was conditioned at room temperature for at least 2 h to release mixed in air. Rigid PU foams were obtained by mixing polyol and isocyanate (pMDI) components with a mechanical stirrer at 2000 rpm for 15 s and the reacting PU foam mass was poured into an open-top mold.
As seen in Table 2, a few of the used reagents are depicted as a range between certain values. This depicts the experimental matrix of the rigid PU foam formulation optimization. Three factors of the rigid PU foam formulations were changed: the content of the newly developed TOFA-based bio-polyols, the content of the low functionality TO_TEOA polyol, and the content of the physical blowing agent c-pentane in part by weight ratios of 0–95, 95–0, and 0–15, respectively. The experiment matrix of the changed factors is depicted in Table 3. Following c-pentane content for each new TOFA-based bio-polyol and TO_TEOA polyol ratios were tested at 0, 3, 6, 9, 12, and 15 pbw. In total, 36 rigid PU foam formulations were tested for each of the four different TOFA-based bio-polyols amounting to 144 tested formulations.
The altered factor influence on rigid PU foam properties was optimized using response surface modeling (RSM) which was done with the help of Design Expert software (Version V12.0.7.0, Stat-Ease, Inc. Minneapolis, MN, USA). The following responses were investigated which were tested according to respective testing standards: apparent density ISO 845:2006, closed cell content ISO 4590:2016, and technological rigid PU foam foaming parameters (start time, string time, tack-free time, and rise time—cup test methodology). A linear or polynomic model was fitted for each response that optimized rigid PU foam formulation in targeted constraints and delivered a desirability surface. The most optimal rigid PU foam formulation and a few others in the area of highest desirability were selected to obtain larger scale rigid PU foam samples to test the thermal conductivity and compression strength. The thermal conductivity was measured according to ISO 8301:1991 at an average temperature of 10 °C (cold plate: 0 °C and hot plate: +20 °C, sample dimensions: 200 × 200 × 30 mm). The compression strength of rigid PU foams was tested perpendicular and parallel to the foaming direction using Zwick/Roell Z100 testing machine (Zwick Roell Group, Ulm, Germany), standard EN ISO 844:2014, maximum load-cell capacity 1 kN, the deformation rate: 10%/min) for cylinder specimens with diameter and height of ~20 mm. Six specimens were analyzed for each formulation. The optimization of rigid PU foam formulation resulted in several systems that could be applied as thermal insulation material in the construction industry.
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Publication 2020
This study employed a randomised, crossover design. The study was conducted in accordance with the Declaration of Helsinki, and ethical approval was granted by the Faculty of Science and Technology Ethics Committee, Anglia Ruskin University (Project Number: FST/FREP/15/567). All participants provided written informed consent prior to study inclusion. All monitoring procedures took place in the Cambridge Centre for Sport and Exercise Sciences, Anglia Ruskin University under controlled conditions.
Participants were required to be healthy, recreationally active runners (training a minimum of 3 days per week with at least 3 months habitual experience, and satisfactorily complete a health screen questionaire) and prepared to comply with study requirements. Ineligible participants were those with a known health condition (including persistent non-exercise related GI issues), current injury, or recent viral infection. Participants were required to only eat foods in conjunction with the lists provided for each 7 day period, and be prepared to weigh food and keep a detailed food log. All participants reported  no known or diagnosed gut disorders, were not currently following a LOWFODMAP, ketogenic or calorie restricted diet, were not currently taking antibiotics or probiotics, and had no known blood disorders or allergies.
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Publication 2019
Antibiotics Caloric Restriction Ethics Committees Faculty Food Hematological Disease Hypersensitivity Injuries Probiotics Screening Virus Diseases
A modified rigid PU foam formulation described by Tu et al. (2007) was used in this study with the components outlined in Table 1.31 The A-side component used in the formulation is polymeric Methyl Diphenyl Diisocyanate (MDI) added to the B-side at an isocyanate index of 110. B-side reactants comprising polyol(s), surfactants, blowing agent, and catalyst were weighed into a 500 mL disposable plastic cup and mixed at 3450 rpm for 10–15 s. The mixture was degassed for 120 s, and then PAPI™ 27 polymeric MDI was rapidly added with continuous stirring for another 10–15 s at a similar speed. The mixture was immediately poured into a wooden mold (11.4 × 11.4 × 21.6 cm3) with an aluminum foil lining, and the foam was allowed to rise and set under ambient conditions (23 °C, 1 atm). The cream times and gel times were recorded to investigate p-CDEA's catalytic effect during the foaming process. The synthesized PUA foams were labeled according to the type and level of polyol substitution (i.e., fossil-based polyol = Voranol® 490 and CO-based polyol = p-CDEA). A PU-V490 labeled foam has no p-CDEA in its formulation (i.e., completely fossil-based) while a PU-p-CDEA foam has none of the Voranol® 490 (i.e., completely bio-based). Further, PU-40-p-CDEA and PU-80-p-CDEA foams have 40 wt% p-CDEA-60 wt% Voranol®490 and 80 wt% p-CDEA-20 wt% Voranol®490 polyols in their formulation, respectively. Two types of surfactants were also used in combination with the different p-CDEA formulations. The prepared foam samples were allowed to cure for seven days before characterization.
Publication 2023
Aluminum Catalysis diphenyl Fungus, Filamentous Isocyanates Muscle Rigidity polymeric 4,4'-diphenylmethane diisocyanate Polymers polyol Surfactants
The solvothermal method is mainly used for directing the formations of various metal oxides, such as ZnO NRs since it is an eco-friendly, high-yield, and simple process [58 (link)]. ZnO@OAm NRs were prepared by the solvothermal method: Zn(acac)2 (1.06 mmol) was mixed and dissolved in 4 mL of TrEG and 4 mL of OAm, under stirring at 30 °C for 15 min. The resulting solution was centrifuged into a Teflon-lined stainless-steel autoclave under a solvothermal polyol process. The reaction was carried out at 200 °C for 8 h. After the solvothermal polyol process, the solution was centrifugation at 5000 rpm for 20 min. The supernatants were discarded, and a white-bronze precipitate was acquired and washed with disolol to remove the untreated precursors. Reaction yield was calculated at 38% based on the metal precursor.
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Publication 2023
Anabolism Centrifugation Dental Alloys Metals Oxides polyol Stainless Steel Teflon

Most recents protocols related to «Polyol»

Different polyol formulations consisting
of glycerol, PA, and CMG were weighed and mixed in an Erlenmeyer flask
according to the mass ratios listed in Table 2. The starting ratio of reactants was determined
stoichiometrically, and subsequent ratios were based on increasing
excess of CMG by a molar increment. The flask was placed on a hot
plate with a magnetic stirrer, and a thermometer clamped on an iron
stand was inserted in the flask. The reaction was done at 120 °C
for 30 min with constant stirring at 1000 rpm. Then the temperature
was increased to 180 °C, and the reaction was allowed to proceed
for 3 h with constant stirring at 1000 rpm. After the reaction, the
products were subjected to vacuum drying for 2 h at 160 °C. The
final polyol products, referred to as CMG-based polyol (CMGPOL), followed
by the mass ratio of CMG in the polyol formulation, were dark brown
liquids that were physically stable at room temperatures. They were
stored in tightly sealed containers.
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Publication 2024
For polyol lipid determination, culture broth was centrifuged (5 min, 17,000 ×g). The cell pellet and polyol lipid were resuspended in acetonitrile. After another centrifugation step (5 min, 17,000 ×g), the acetonitrile, including dissolved polyol lipid, is separated from the cell fragments. The determination is carried out gravimetrically by evaporating the acetonitrile in pre-weighed glass vials using a speed vac at medium temperature (Savant Instruments, Speed Vac SC-100, Farmingdale, New York, United States). All wells from cultivations in MTPs undergo complete processing, followed by an additional acetonitrile rinse. After rinsing, the acetonitrile was used to resuspend the cell pellet, and polyol lipid after the first centrifugation step. In the case of samples obtained from the bioreactor, 1 mL of culture broth is utilized for each sample, with an accompanying 1 mL of acetonitrile.
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Publication 2024
CGE (0.1 mol, 35.6 g) and DEA (0.1 mol, 10.5 g) were added to a four-port flask equipped with a stirring paddle. The reaction needed to be performed at 70 °C for 4 h under N2. After the reaction, the upper light yellow organic phase was dissolved and extracted using ethyl acetate and subsequently washed with saturated saline and deionized water to neutral. Subsequently, anhydrous sodium sulfate was added to remove water. After night drying and filtration followed by rotary evaporation to remove the excess solvent, cardanol amine polyol was obtained, named CAP.
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Publication 2024
The bio-polyol was synthesized by hydroxylation of sunflower oil in one conversion step using a mixture of hydrogen peroxide and formic acid followed the method reported in literature.20 (link) Sunflower oil sample, HCOOH acid catalyst with specified ratio was added to the conical flask, and mixed well by magnetic stirrer. H2O2 solution with certain volume was slowly added to the above conical flask, stirred until obtaining homogeneous solution. Next, closed the conical flask was heated to the required temperature by heated magnetic stirrer. After the reaction time, the separating funnel was used to obtain the bio-polyol product. In particular, two layer of reaction mixture was separated by funnel and the upper layer was washed 2–3 times with a solvent consisting of 10% Na2CO3 solution and acetone (ratio 60 : 40 in volume). The liquid layer that contained bio-polyol product was then washed with a washing solution of water and acetone until the pH of 7. At the end of the washing stage, most of the acetone and water were separated by a separating funnel. Then, rotary distillation apparatus was used to remove the remaining acetone and water in the product. The final product was completely dried with anhydrous Na2SO4 and anhydrous silica in a desiccator for 24 h. The hydroxylation process was repeated twice, and the variance was recorded.
Publication 2024
Following the procedure described by Abril-Milán et al. [11] (link) the acid number of SBF and SBFpolyol was determined. In order to ascertain the composition, a thoroughly mixed test sample (5 g for shea butter and 10 g for polyol) was placed within a 250-mL Erlenmeyer flask. The process entailed the consecutive addition of 50 mL of hot ethanol (EtOH) and 1 mL of a 1% phenolphthalein solution.
Afterwards, the combination was cooked on a hotplate until it reached its boiling point and then kept at that temperature for a duration of 5 minutes. Eventually, the flask was brought down, and the mixture was promptly titrated (while it was still hot) using 0.1M NaOH with vigorous stirring, until the moment when the transparent solution changed to a pink tint. The volume of 0.1M NaOH was used to calculate the acid value according to the provided formula:
V is the volume in ml of standard NaOH consumed, M is the molarity of the NaOH, and W is the weight of the sample.
Publication 2024

Top products related to «Polyol»

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1,4-butanediol is a colorless, viscous chemical compound that is commonly used as a laboratory reagent. It has a molecular formula of C4H10O2 and a molecular weight of 90.12 g/mol. 1,4-butanediol is a versatile compound that can be used for various applications in research and development.
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Lupranat M20S is a polyol product manufactured by BASF. It is a liquid polyol designed for use in polyurethane foam formulations.
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The Praccel L205AL is a laboratory equipment product manufactured by Daicel. It is designed to perform specific functions in a laboratory setting. However, without more detailed information about its core function, I cannot provide a description that maintains an unbiased and factual approach. Description not available.
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Diethylene glycol is a clear, colorless, odorless, and viscous liquid. It is a common ingredient in various industrial and laboratory applications, primarily serving as a solvent, antifreeze, and humectant.
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Acetone is a colorless, volatile, and flammable liquid. It is a common solvent used in various industrial and laboratory applications. Acetone has a high solvency power, making it useful for dissolving a wide range of organic compounds.

More about "Polyol"

Polyols are a diverse class of organic compounds characterized by the presence of multiple hydroxyl (-OH) groups.
These versatile molecules find a wide range of applications across various industries, from the production of plastics and adhesives to personal care products.
Polyols can be derived from natural sources, such as plant oils and sugars, or synthesized from petrochemical feedstocks like dibutyltin dilaurate, ethylene glycol, and diethylene glycol.
The unique properties of polyols, including low toxicity, high viscosity, and water solubility, make them highly valuable in numerous applications.
Researchers in the field of polyol science focus on optimizing synthesis methods, improving product quality, and developing novel uses for these multifunctional compounds.
PubCompare.ai's AI-driven platform offers a powerful solution for polyol research optimization.
By providing easy access to relevant protocols from literature, preprints, and patents, the platform enables researchers to identify the best protocols and products, ultimately enhancing the reproducibility and efficiency of their work.
Beyond polyols, related compounds such as 1,4-butanediol, Lupranat M20S, Placcel® FM-3, Praccel L205AL, and hydrogen peroxide are also of interest in this field, as they may be used in the synthesis or applications of polyols.
By leveraging the insights and tools offered by PubCompare.ai, researchers can navigate the complex landscape of polyol research and unlock new possibilities for these versatile and impactful compounds.