Butanes
They are commonly used as fuel gases, propellants, and refrigerants due to their low boiling points and high flammability.
Butanes can occur naturally in crude oil and natural gas deposits, or they can be produced synthetically through the refining of petroleum.
Researcheres can utilize PubCompare.ai's AI-driven tools to efficiently locate, compare, and optimize protocols relating to the use and analysis of butanes, enhanceing the accuracy and productivity of their butanes-focused projects.
Most cited protocols related to «Butanes»
Most recents protocols related to «Butanes»
Example 37
To improve inhibition potency relative to FAAH, various portions of the t-TUCB molecule were modified to identify potential FAAH pharmacophores. The 4-trifluoromethoxy group on t-TUCB was modified to the unsubstituted ring (A-3), 4-fluorophenyl (A-2) or 4-chlorophenyl (A-26). Potency on both sEH and FAAH increased as the size and hydrophobicity of the para position substituent increased, with 4-trifluoromethoxy being the most potent on both enzymes. Substituting the aromatic ring for a cyclohexane (A-3) or adamantane (A-4) resulted in a complete loss in activity against FAAH. Results are summarized in Table 1 below.
Next, the center portion of the molecule was modified to further investigate the specificity of t-TUCB on FAAH. Switching the cyclohexane linker to a cis conformation (A-5) resulted in a 20-fold loss of potency while removing the ring and replacing it with a butane chain (A-6) resulted in a completely inactive compound. While this suggests the compound must fit a relatively specific conformation in the active site to be active, we found the aromatic linker had essentially the same potency on FAAH (A-7). Although many potent urea-based FAAH inhibitors have a piperidine as the carbamoylating nitrogen, the modification to piperidine here reduced potency 13-fold. Results are summarized in Table 2 below.
Since none of the modifications at this point improved potency towards FAAH, we focused on the benzoic acid portion of the molecule as shown in Table 3. To determine the importance of the terminal acid, the corresponding aldehyde (A-20) and alcohol (A-24) in addition to the amide (A-19) and nitrile (A-11) were tested. While the amide had slightly improved potency, the more reduced forms of the acid (A-20 and A-24) and amide (A-11) had substantially less activity on FAAH. Converting the benzoic acid to a phenol (A-21) increased potency while the anisole (A-22) was completely inactive. Since the amide and acid appeared to be active, the amide bioisostere oxadiazole (A-25) was tested and had 38-fold less potency than the initial compound.
Since the substrates for FAAH tend to be relatively hydrophobic lipids, we speculated that conversion of the acid and primary amide to the corresponding esters or substituted amides would result in improved potency. The methyl ester (A-12) had 4-fold improved potency relative to the acid. Improving the bulk of the ester with an isopropyl group (A-13) results in a 11-fold loss in potency relative to the methyl ester. However, the similar potency of the benzyl ester (A-14) to the methyl ester demonstrates the bulk but not the size affects potency. Reversing the orientation of the ester (A-23) reduces the potency 3.4-fold. Relative to the primary amide, the methyl (A-18), ethanol (A-15) and glycyl (A-16) amides were all slightly less potent; however, the benzyl amide (A-27) was substantially less potent (16-fold). Generating the methyl ester of the glycyl amide (A-17) increased the potency 4-fold compared to the corresponding acid.
the experiments have been described in detail in an earlier publication,30 (link) with some modifications to the reaction procedure
for propane, as well as the analysis procedure by gas chromatography
(
product mixture. Briefly, a Parr reactor is used with a Teflon insert
in the reactor along with a shaft and a thermowell coated with Teflon
to prevent ozone decomposition on the metal surfaces.
A dioxygen
stream is used to generate a mixture of ozone and dioxygen with the
desired ozone mole fraction by an Atlas ozone generator and charged
into a reservoir equipped with a pressure transducer.57 (link) Ar is then added into the reservoir to a desired pressure.
Unless otherwise mentioned, the mixture contains about 5% O3 and 45% O2, with the balance being Ar. A Teflon-lined
Parr vessel is evacuated at 80 °C under vacuum. The reactor is
cooled and charged with the desired amounts of liquid alkanes (0.3
mol total alkanes) from an ISCO syringe pump cooled to 10 °C.
An option to direct the liquid alkane stream through a sample loop
containing distilled water is provided to meter in controlled amounts
of water. The reactor stirrer is set at 1000 rpm to allow the reactor
to stabilize at the laboratory temperature of around 24–25
°C. Throughout a semi-batch run, the O2 + O3 + Ar mixture is supplied continuously to the reactor via a pressure
regulator maintained at a constant pressure. The reaction conditions
are provided in figure captions. The alkanes that escape with the
gas phase are partially condensed in a cold trap held around −60
to −50 °C and ambient pressure to concentrate the CO2. The gas from the condenser is collected in Tedlar sample
bags. At the end of a run, the reactor is placed in an ice bath kept
in a freezer at −18 °C. At this temperature, the vapor
pressures of all compounds remaining in the reactor are very low (
methanol is added into the reactor, and the reactor is kept at around
0–4 °C to allow the remaining alkanes to vaporize and
be condensed in the cold trap. The trap is maintained at around −60
to −50 °C for butanes, and around −90 °C when
propane is present. After adding 2-pentanone as an internal standard,
the methanolic liquid sample is injected into an Agilent 7890A GC
equipped with a flame ionization detector (FID) and a HP-PLOT/Q column
to resolve ≥C2 products. The methanolic liquid sample
is also added to D2O with maleic acid as an internal standard
to quantify formic acid by 1H NMR spectroscopy. The gas
samples collected in Tedlar bags were injected into another GC equipped
with a thermal conductivity detector to analyze the CO2 and an FID to analyze the hydrocarbons. More details of the GC/FID
analytical methods, including a sample chromatogram, are provided
in
The details of
estimating alkane conversion (X), molar product selectivity,
and O3 utilization (U), as well as their
confidence intervals, are provided
in
is characterized by the ratio of utilized oxidizing equivalents from
ozone/theoretical maximum oxidizing equivalents.
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More about "Butanes"
These versatile compounds are commonly utilized as fuel gases, propellants, and refrigerants, thanks to their low boiling points and high flammability.
Butanes can be found naturally in crude oil and natural gas deposits, or they can be synthesized through the refining of petroleum.
Researchers can leverage the power of PubCompare.ai's AI-driven tools to efficiently locate, compare, and optimize protocols related to the use and analysis of butanes, enhancing the accuracy and productivity of their butanes-focused projects.
These tools can help identify the most accurate and reproducible protocols, drawing from a vast database of literature, pre-prints, and patents.
Beyond butanes, researchers may also find PubCompare.ai's tools useful for exploring other related compounds and techniques, such as bovine serum albumin (BSA), fetal bovine serum (FBS), triethylamine, diacetyl, Wiley mills for sample preparation, GC-FID for analytical methods, dibutyltin dilaurate, dimethylolpropionic acid, and DMSO or 1,4-butanediol as solvents.
By leveraging the power of AI-driven protocol optimization, researchers can ensure the accuracy and efficiency of their butanes-related projects, leading to more robust and insightful findings.