Primer pairs for RT-qPCR amplification were designed based on selected sequences using Beacon Designer 7.0 software (Premier Biosoft International, Palo Alto, California, USA) with a melting temperature between 60–62°C, 20–26 bp and about 50% GC content. Amplicon lengths were optimized to 103–146 bp to ensure optimal polymerization efficiency and minimize the impact of RNA integrity on relative quantification of gene expression [65 (link)]. MFOLD software [66 (link)] was subsequently used to evaluate the target sequences amplified by the primer pairs to avoid the formation of secondary structures at the site of primer binding. The primers were further used to query peach EST database with BLASTN to confirm the identity of the genes. Before RT-qPCR, each primer pair was tested via standard RT-PCR to check for size specificity of the amplicon by 2.5% agarose gel electrophoresis and ethidium bromide staining. In addition, target amplicons were sequenced to confirm specificity of the PCR products. The primer sequences, amplicon sizes, and melting temperatures of all PCR products were indicated in Table
Polymerization
This process is fundamental to the production of a wide range of materials, including plastics, rubbers, and synthetic fibers.
Polymerization can occur through various mechanims, such as addition polymerization, condensation polymerization, and ring-opening polymerization, depending on the specific monomers and conditions involved.
The study of polymerization is an important field of research, with applications in materials science, engineering, and biotechnology.
Researchers in this area aim to optimize polymerization processes to enhance the properties and performance of polymeric materials for diverse applications.
Most cited protocols related to «Polymerization»
Primer pairs for RT-qPCR amplification were designed based on selected sequences using Beacon Designer 7.0 software (Premier Biosoft International, Palo Alto, California, USA) with a melting temperature between 60–62°C, 20–26 bp and about 50% GC content. Amplicon lengths were optimized to 103–146 bp to ensure optimal polymerization efficiency and minimize the impact of RNA integrity on relative quantification of gene expression [65 (link)]. MFOLD software [66 (link)] was subsequently used to evaluate the target sequences amplified by the primer pairs to avoid the formation of secondary structures at the site of primer binding. The primers were further used to query peach EST database with BLASTN to confirm the identity of the genes. Before RT-qPCR, each primer pair was tested via standard RT-PCR to check for size specificity of the amplicon by 2.5% agarose gel electrophoresis and ethidium bromide staining. In addition, target amplicons were sequenced to confirm specificity of the PCR products. The primer sequences, amplicon sizes, and melting temperatures of all PCR products were indicated in Table
Most recents protocols related to «Polymerization»
EXAMPLE 1
In an AISI 316 steel vertical autoclave, equipped with baffles and a stirrer working at 570 rpm, 3.5 liter of demineralized water were introduced. The temperature was then brought to reaction temperature of 80° C. and the selected amount of 34% w/w aqueous solution of cyclic surfactant of formula (VI) as defined above, with Xa=NH4, was added. VDF and ethane were introduced to the selected pressure variation reported in Table 1. A gaseous mixture of TFE-VDF in the molar nominal ratio reported in Table 1 was subsequently added via a compressor until reaching a pressure of 20 bar. Then, the selected amount of a 3% by weight water solution of sodium persulfate (NaPS) as initiator was fed. The polymerization pressure was maintained constant by feeding the above mentioned TFE-VDF while adding the PPVE monomer at regular intervals until reaching the total amount indicated in the table 1.
When 1000 g of the mixture were fed, the reactor was cooled at room temperature, the latex was discharged, frozen for 48 hours and, once unfrozen, the coagulated polymer was washed with demineralized water and dried at 160° C. for 24 hours.
The composition of the obtained polymer F-1, as measured by NMR, was Polymer (F-1)(693/99): TFE (69.6% mol)—VDF (27.3% mol)—PPVE (2.1% mol), having melting point Tm=218° C. and MFI=5 g/10′.
The procedure of example 1 was repeated, by introducing the amount of ingredients indicated in the third column of Table 1.
The composition of the obtained polymer P-1, as measured by NMR, was Polymer (C-1)(693/67): TFE (71% mol)—VDF (28.5% mol)—PPVE (0.5% mol), having melting point Tm=249° C. and MFI=5 g/10′.
EXAMPLE 2
The procedure of example 1 was repeated, by introducing the amount of ingredients indicated in the second column of Table 1.
The composition of the obtained polymer F-2, as measured by NMR, was Polymer (F-1)(693/100): TFE (68% mol)—VDF (29.8% mol)—PPVE (2.2% mol), having melting point Tm=219° C. and MFI=1.5 g/10′.
In an AISI 316 steel horizontal reactor, equipped with a stirrer working at 42 rpm, 56 liter of demineralized water were introduced. The temperature was then brought to reaction temperature of 65° C. and the selected amount of 40% w/w aqueous solution of cyclic surfactant of formula (VI) as defined above, with X1=NH4, was added. VDF and ethane were introduced to the selected pressure variation reported in Table 1.
A gaseous mixture of TFE-VDF in the molar nominal ratio reported in Table 1 was subsequently added via a compressor until reaching a pressure of 20 bar.
Then, the selected amount of a 0.25% by weight water solution of sodium persulfate (NaPS) as initiator was fed. The polymerization pressure was maintained constant by feeding the above mentioned TFE-VDF while adding the PPVE monomer at regular intervals until reaching the total amount indicated in the table 1.
When 16000 g of the mixture were fed, the reactor was cooled at room temperature, the latex was discharged, frozen for 48 hours and, once unfrozen, the coagulated polymer was washed with demineralized water and dried at 160° C. for 24 hours. The composition of the obtained polymer C-2, as measured by NMR, was Polymer (C-2)(SA1100): TFE (70.4% mol)—VDF (29.2% mol)—PPVE (0.4% mol), having melting point Tm=232° C. and MFI=8 g/10′.
EXAMPLE 3
The procedure of Comparative Example 2 was repeated, by introducing the following changes:
-
- demineralized water introduced into the reactor: 66 litres;
- polymerization temperature of 80° C.
- polymerization pressure: 12 abs bar
- Initiator solution concentration of 6% by weight
- MVE introduced in the amount indicated in table 1
- Overall amount of monomers mixture fed in the reactor: 10 000 g, with molar ratio TFE/VDF as indicated in Table 1.
All the amount of ingredients are indicated in the fifth column of Table 1.
The composition of the obtained polymer (C-3), as measured by NMR, was Polymer (C-3)(693/22): TFE (72.1% mol)—VDF (26% mol)—PMVE (1.9% mol), having melting point Tm=226° C. and MFI=8 g/10′.
The results regarding polymers (F-1), (F-2) of the invention, and comparative (C-1), (C-2) and (C-3) are set forth in Table 2 here below
In particular, the polymer (F) of the present invention as notably represented by the polymers (F-1), (F-2), surprisingly exhibits a higher elongation at break at 200° C. as compared to the polymers (C-1) and (C-2) of the prior art.
Also, the polymer (F) of the present invention as notably represented by the polymers (F-1), (F-2), despite its lower tensile modulus, which remains nevertheless in a range perfectly acceptable for various fields of use, surprisingly exhibits a higher strain hardening rate by plastic deformation as compared to the polymers (C-1) and (C-2) of the prior art.
Finally, the polymer (F) of the present invention as notably represented by the polymers (F-1) and (F-2) surprisingly exhibits higher environmental stress resistance when immersed in fuels as compared to the polymers (C-1) and (C-2) of the prior art.
Yet, comparison of polymer (F) according to the present invention with performances of polymer (C-3) comprising perfluoromethylvinylether (FMVE) as modifying monomer shows the criticality of selecting perfluoropropylvinylether: indeed, FMVE is shown producing at similar monomer amounts, copolymer possessing too high stiffness, and hence low elongation at break, unsuitable for being used e.g. in O&G applications.
Example 28
A typical protocol used for the synthesis of the PNAEP67-PnBA500 diblock copolymer was as follows: PNAEP67 macro-CTA (0.185 g, 14.6 μmol), deionised water (4.501 g, corresponding to a 20% w/w solution) and KPS (1.320 mg, 4.9 μmol; PNAEP67/KPS=3.0) were weighed into a 10 mL round-bottom flask charged with a magnetic flea. HCl (10 μL, 0.2 M) was added to reduce the pH to 3.0. This flask was then immersed in an ice bath, and the solution was degassed with nitrogen for 30 min. nBA (1.500 g) was weighed into a separate 14 mL vial and degassed with nitrogen in an ice bath for 30 min. An AsAc stock solution (0.01% w/w) was weighed into a second 14 mL vial and degassed with nitrogen in an ice bath for 30 min. After 30 min nBA (1.05 ml, 7.32 mmol; target DP=500) was added to the flask using a degassed syringe and needle under nitrogen. The flask contents were then stirred vigorously to ensure thorough mixing and degassed for 5 min before being immersed in an oil bath set at 30° C. After 1 min, AsAc (0.09 ml, 4.9 μmol; KPS/AscAc molar ratio=1.0) was added to the flask. The nBA polymerisation was allowed to proceed for 1 h before being quenched by exposing the reaction solution to air and immersing the reaction vial in an ice bath. 1H NMR spectroscopy analysis of the disappearance of vinyl signals indicated a final nBA conversion of 99%. Chloroform GPC analysis of this copolymer indicated a Mn of 86.6 kg mol−1 and an Mw/Mn of 1.56. Other diblock copolymer compositions were obtained by adjusting the nBA/PNAEP67 molar ratio.
Example 1
This example describes an exemplary nanostructure (i.e. nanocomposite tecton) and formation of a material using the nanostructure.
A nanocomposite tecton consists of a nanoparticle grafted with polymer chains that terminate in functional groups capable of supramolecular binding, where supramolecular interactions between polymers grafted to different particles enable programmable bonding that drives particle assembly (
Once synthesized, nanocomposite tectons were functionalized with either diaminopyridine-polystyrene or thymine-polystyrene were readily dispersed in common organic solvents such as tetrahydrofuran, chloroform, toluene, and N,N′-dimethylformamide with a typical plasmonic resonance extinction peak at 530-540 nm (
A key feature of the nanocomposite tectons is that the sizes of their particle and polymer components can be easily modified independent of the supramolecular binding group's molecular structure. However, because this assembly process is driven via the collective interaction of multiple diaminopyridine and thymine-terminated polymer chains, alterations that affect the absolute number and relative density of diaminopyridine or thymine groups on the nanocomposite tecton surface impact the net thermodynamic stability of the assemblies. In other words, while all constructs should be thermally reversible, the temperature range over which particle assembly and disassembly occurs should be affected by these variables. To better understand how differences in nanocomposite tecton composition impact the assembly process, nanostuctures were synthesized using different nanoparticle core diameters (10-40 nm) and polymer spacer molecular weights (3.7-11.0 kDa), and allowed to fully assemble at room temperature (˜22° C.) (
From these data, two clear trends can be observed. First, when holding polymer molecular weight constant, Tm increases with increasing particle size (
All nanocomposite tectons possess similar polymer grafting densities (i.e. equivalent areal density of polymer chains at the inorganic nanoparticle surface,
Conversely, for a fixed inorganic particle diameter (and thus constant number of polymer chains per particle), increasing polymer length decreases the areal density of diaminopyridine and thymine groups at the nanocomposite tecton periphery due to the “splaying” of polymers as they extend off of the particle surface, thereby decreasing Tm in a manner consistent with the trend in
Importantly, because the nanocomposite tecton assembly process is based on dynamic, reversible supramolecular binding, it should be possible to drive the system to an ordered equilibrium state where the maximum number of binding events can occur. The particle cores and polymer ligands are polydisperse (
To test this hypothesis, multiple sets of assembled nanocomposite tectons were thermally annealed at a temperature just below their Tm, allowing particles to reorganize via a series of binding and unbinding events until they reached the thermodynamically most stable conformation. The resulting structures were analyzed with small angle X-ray scattering, revealing the formation of highly ordered mesoscale structures where the nanoparticles were arranged in body-centered cubic superlattices (
Example 5
In some embodiments, the disclosed ECP has a formula of
The ECP-5 is synthesized by preparing a naphthalene-containing reaction unit and then polymerizing it with an AcDOT unit. The detail method includes the following steps:
Step 5-1: preparing naphthalene-containing reaction unit (compound 10) by two steps.
To a solution of compound 11 in dichloromethane was added dropwise a solution of bromine in dichloromethane over 15 minutes at −78° C. The reaction mixture is stirred for 2 hours at −78° C. and then warmed gradually to room temperature and stay at room temperature for an additional 2 hours. The excess bromine was quenched by saturated aqueous sodium sulfite solution and stirred for 2 hours at room temperature. After extraction with dichloromethane, the combined organic layer was washed with brine, dried over sodium sulfate, and concentrated in vacuum.
Compound 12 is dissolved in DMF under N2, K2CO3 is added to the solution, and the reaction mixture is stirred for 15 minutes, after which 2-ethylexyl bromide is added. The reaction mixture is stirred at 100° C. overnight. The reaction is stopped and cooled down to room temperature. The solvent is removed in vacuum, and the residue is dissolved in diethyl ether. The organic phase is washed with water, and the aqueous phases are extracted with ethyl acetate. The combined organic phases are dried by vacuum.
Step 5-2: polymerization: The polymerization method is similar to that in step 1-1, only differs on the reaction units. The reaction units here are the naphthalene-containing reaction unit (compound 10) and AcDOT (compound 8).
Example 23
The RAFT polymerization of NIPAM was conducted in an oil bath set to 22° C., which is below the LCST of PNIPAM homopolymer (˜32° C.). NIPAM conversions of at least 99% were achieved for all PNAEP95-PNIPAMy diblock copolymers within 1 h at this temperature, as judged by 1H NMR studies conducted in D2O. DMF GPC analysis of this series of PNAEP95-PNIPAMy diblock copolymers indicated a monotonic increase in Mn with increasing PNIPAM DP. Relatively low dispersities (Mw/Mn<1.40) were observed in all cases, indicating reasonably good RAFT control. Moreover, comparison of the GPC traces obtained for these PNAEP95-PNIPAMy diblock copolymers with that of the precursor PNAEP95 macro-CTA indicated relatively high blocking efficiencies.
Top products related to «Polymerization»
More about "Polymerization"
This crucial process is central to the production of a vast array of essential materials, including plastics, rubbers, synthetic fibers, and more.
Polymerization can occur through various mechanisms, such as addition polymerization, condensation polymerization, and ring-opening polymerization, depending on the specific monomers and conditions involved.
The study of polymerization is a vital field of research, with applications spanning materials science, engineering, and biotechnology.
Researchers in this area aim to optimize polymerization processes to enhance the properties and performance of polymeric materials for diverse applications.
This includes exploring techniques like Matrigel, a complex extracellular matrix material used in cell culture, and Glutaraldehyde, a crosslinking agent employed in the polymerization of proteins.
Advanced tools like the Tubulin Polymerization Assay Kit and H-7650 can be used to analyze and monitor the polymerization of key biomolecules, such as tubulin and actin, which are crucial components of the cytoskeleton.
Additionally, the use of fetal bovine serum (FBS) and Cytochalasin D, a compound that disrupts actin polymerization, can provide insights into the dynamics of the cytoskeleton and its role in cellular processes.
Optimizing polymerization processes often involves the use of antioxidants, such as Irganox® 1076, to enhance the stability and durability of polymeric materials.
Furthermore, the versatility of DMSO, a common solvent, makes it a valuable tool in polymerization research, particularly in the context of Actin Polymerization Biochem Kits.
By leveraging the power of AI-driven platforms like PubCompare.ai, researchers can efficiently locate the best protocols from literature, pre-prints, and patents, ultimately enhancing the reproducibility and accuracy of their polymerization research.
This ensures that their work is not only informative and clear, but also efficient and reliable.