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Hydrocarbons

Hydrocarbons are a vast and diverse class of organic compounds composed solely of carbon and hydrogen atoms.
They are the simplest organic molecules and serve as the fundamental building blocks for a wide range of fuels, chemicals, and materials essential to modern industry and society.
Hydrocarbons can exist in various forms, including alkanes, alkenes, alkynes, and aromatic compounds, each with unique structural and chemical properties.
These versatile molecules play a crucial role in the energy, petrochemical, and pharmaceutical industries, as well as in many everyday products.
Researchers and scientists continually explore the production, properties, and applications of hydrocarbons to advance our understanding and utilization of this vital group of compounds.
Whther you're investigating hydrocarbon-based fuels, polymers, or other derivatives, the comprehensive knwoledge of this topic can unlock new discoveries and innovations.

Most cited protocols related to «Hydrocarbons»

Primers applied in analysing of gut content of predators should ideally target short sequences of multiple-copy DNA because of the degraded nature of the prey derived sequences [13 (link),16 (link),17 ,36 (link)]. The ribosomal DNA is therefore often used as a target for PCR amplification in diet studies because ribosomal DNA (rDNA) genes are repeated tandemly in high copy numbers and are highly conserved within species [37 (link)]. We designed 'universal' PCR primers that amplify a short, but fairly variable region of the 28S rDNA from all eukaryotes tested. We also designed three blocking primers intended to bind to the Euphausia superba sequence amplified by the universal primers. The primers used in this study are given in Table 1 and shown aligned with the krill sequence in Figure 2.
The blocking primer, 'Short28SR-blkKrill3'c3' overlapped with the 3' end of the reverse universal primer, but extended into krill-specific sequence and was modified with a C3 spacer at the 3'-end (Figure 2). We needed a modification which was 100% synthesized (i.e. no oligos missing it) and which was stable (i.e. no degradation or enzymatic removing of the modification after synthesis). Even if just a small percentage of the blocking primers were to prime amplification of predator DNA as a result of not having the 3' modification, this would render the procedure unworkable. C3 spacer (3 hydrocarbons) CPG is a standard primer modification available from most suppliers of custom oligonucleotides. Adding this modification to the 3'-end of an oligonucleotide prevents elongation during a PCR without noticeably influencing its annealing properties. Because oligos are synthesized from a 3' to 5' direction, all molecules will be modified with the 3' modification. Modifying the 3'- end with a phosphate group (as chosen by Liles et al. [35 (link)]), a phosphate ester, or using an inverted 3'-3' linkage would also prevent elongation. However, side reactions during deprotection of the oligonucleotide or enzymatic impurities may free the 3'-hydroxyl group to a small extent, and these methods are not so effective in blocking as C3 spacers CPG [38 (link),39 (link)].
Because finding an appropriate binding site for a species specific primer next to a binding site of a universal primer is often difficult, a krill specific blocking primer, Short28SF-DPO-blkKrill overlapping with the 3'end of the forward universal primer and having an internal modification of five deoxyinosine (dI) molecules in addition to the C3 spacer modification was also designed (Figure 2). Very long conventional oligonucleotides often do not work. In general, primers longer than 25 bases are rarely used since their Tms can be over 70°C, which is too high for effective PCR cycling [40 (link)]. Long primers also often generate many non-specific bands resulting from non-specific annealing. A dual priming oligonucleotide (DPO) [41 (link)] contains two separate priming regions joined by a polydeoxyinosine linker. DPOs does not suffer from the limitations of a high Tm since the linker assumes a bubble-like structure resulting in two primer segments with distinct annealing properties. Furthermore, the bubble-like structure of linker efficiently prevents primer-dimer and hairpin structure formation [41 (link)].
The Short28SR-blkKrill3'c3 and the Short28SF-DPO-blkKrill blocking primers were both designed to prevent annealing of the unmodified version of the universal primer on krill sequences. Further a third krill specific blocking primer situated between the two universal primers was tested (Figure 2). This was an "elongation arrest" primer ([42 (link)]; Figure 1) and also had a C3 spacer at its 3' end.
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Publication 2008
2',5'-oligoadenylate Binding Sites Cardiac Arrest deoxyinosine Diet DNA, Ribosomal Enzymes Esters Eukaryota Euphausia Euphausiacea Genes Hydrocarbons Hydroxyl Radical Oligonucleotides Phosphates
Ions were generated by a nanoelectrospray ionization (nanoESI) source (3000 V) using a chemically etched emitter (20 μm i.d.) connected to a 30 μm i.d. fused-silica capillary (Polymicro Technologies, Phoenix, AZ) through a zero volume stainless steel union (Valco Instrument Co. Inc., Houston, TX). Sample solutions were infused at a flow rate of 0.3 μL/min. Ions were introduced into the first stage of vacuum through a heated (130 °C) 500 μm i.d. stainless steel capillary (Figure 1A). After exiting the capillary, ions were accumulated and stored for 25 ms by an ion funnel trap (IFT, 950 kHz and ~200 Vpp) at 1.85 to 3.95 Torr and then released over 486 μs.64 (link) The ion inlet capillary was offset from the center axis of the IFT by 6 mm to minimize the transmission of neutrals through the IFT and conductance-limiting orifice, as well as to effectively eliminate gas dynamic effects in the SLIM chamber. Upon exiting the trapping region of the IFT, ions pass through a 2.5 cm long converging region of the IFT and are transported through a conductance-limiting orifice (2.5 mm i.d.) into the SLIM module chamber. The TW SLIM chamber was maintained at 2–4 Torr nitrogen filtered through hydrocarbon and moisture traps. A differential positive pressure of ~50 mTorr was also used to further prevent neutrals from entering the SLIM chamber. After drifting through the TW SLIM module, a 15 cm long rear ion funnel (820 kHz and ~120 Vpp) with a 23 V/cm DC gradient was used to focus the ion beam through a conductance limiting orifice (2.5 mm i.d.) into the differentially pumped region (460 mTorr) containing a short RF-only quadrupole (1 MHz and ~130 V). Ions are then transmitted into an Agilent 6224 TOF MS equipped with a 1.5 m flight tube (Agilent Technologies, Santa Clara, CA). Data were acquired using a U1084A 8-bit ADC digitizer (Keysight Technologies, Santa Rosa, CA) and processed using in-house control software written in C#.
Publication 2016
Capillaries Epistropheus Hydrocarbons Ions Nitrogen Pressure Rosa Silicon Dioxide Stainless Steel Vacuum
All experimental protocols for the procedures with rats were pre-approved by the Washington State University Animal Care and Use Committee (IACUC approval # 02568-026). The University Department of Environmental Health and Safety approved all the protocols for the use of hazardous chemicals in this experiment. Sprague Dawley SD female and male rats of an outbred strain (Harlan) at about 70 and 100 days of age were maintained in ventilated (up to 50 air exchanges/hour) isolator cages (cages with dimensions of 10 ¾″ W×19 ¼″ D×10 ¾″ H, 143 square inch floor space, fitted in Micro-vent 36-cage rat racks; Allentown Inc., Allentown, NJ) containing Aspen Sani chips (pinewood shavings from Harlan) as bedding, and a 14 h light: 10 h dark regimen, at a temperature of 70 F and humidity of 25% to 35%. The mean light intensity in the animal rooms ranged from 22 to 26 ft-candles. Rats were fed ad lib with standard rat diet (8640 Teklad 22/5 Rodent Diet; Harlan) and ad lib tap water for drinking. During the procedures, rats were held in an animal transfer station (AniGard 6VF, The Baker Company, Sanford, ME) that provided an air velocity of about 0.5 inch.
At proestrus as determined by daily vaginal smears, the female rats, (90 days) were pair-mated with male rats (120 days). On the next day, the females were separated and their vaginal smears were examined microscopically and if they were sperm-positive (day 0) the rats were tentatively considered pregnant and then weighed with a digital animal weighing balance to monitor increases in body weight. Vaginal smears were continued for monitoring diestrus status in these rats until day 7. On embryonic day 7 (E-7) these females were weighed to determine if there was a significant increase in (greater than about 10 g) body weight, to confirm pregnancy in sperm-positive females. These pregnant rats were then given daily intraperitoneal injections of any one of the following single chemicals or mixtures with an equal volume of sesame oil (Sigma) on days E-8 through E-14 of gestation [43] (link). Treatment groups were Control, Pesticide (Permethrin+DEET), Plastics (Bisphenol-A, DBP and DEHP), Dioxin (TCDD), and Jet Fuel (JP8 hydrocarbon). The pregnant female rats treated with various mixtures were designated as the F0 generation. When there was a drop in the litter size and the sex ratio of pups in F1 generation of Plastics group, another treatment group was included with only half the dose of Bisphenol-A, DBP and DEHP and this group was designated ‘Low Dose Plastics’ group. Doses, percent of oral LD50, and sources of chemicals for the compounds are given in Table S1A.
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Publication 2012
Animals ARID1A protein, human bisphenol A Body Weight DEET Diestrus Diet Diethylhexyl Phthalate DNA Chips Embryo Females Hazardous Chemicals Humidity Hydrocarbons Injections, Intraperitoneal Institutional Animal Care and Use Committees jet fuel A Light Males Permethrin Pesticides Pregnancy Pregnant Women Proestrus Rattus norvegicus Rodent Safety Sesame Oil Sperm Strains Tetrachlorodibenzodioxin Treatment Protocols Vaginal Smears
The MassTRIX webserver is written in Perl using CGI for dynamic content representation and runs on an Apache2 web server (version 2.2.11).
A calibrated mass list, consisting of tab separated masses, intensity values and an additional unique identifier, like an ID or a retention time, serves as main input for MassTRIX. These masses are compared within a certain error range against the theoretical adducts of compounds from different metabolic databases. The default database is a combination of KEGG [4] (link), [5] (link), HMDB [6] (link) and LipidMaps [7] (link) with isotopic peaks. As alternatives the same combination without isotopic peaks, KEGG expanded lipids (where all residues R in formulas, are exchanged by hydrocarbon chains of different lengths), LipidMaps alone for lipidomics and MetaCyc [8] (link) as other databases or a separate m/z list are possible. For the analysis of gene expression data from Affymetrix arrays, R (version 2.10) with the gcrma package are used. Affymetrix identifiers are mapped to the respective KEGG ontology (KO) numbers for visualization on metabolic pathway maps. Correctly annotated KEGG metabolites and KO’s are colored on the respective pathways of a chosen organism by calling the KEGG API. Additionally, enzymes of interest, submitted either as EC-numbers or KEGG identifiers can be highlighted. The obtained maps are fully clickable and cross-linked between the different result pages. Different jobs can be compared on pathway or compound level and all results are downloadable.
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Publication 2012
Diet, Formula Enzymes Gene Expression Profiling Hydrocarbons Isotopes Lipids Microtubule-Associated Proteins Retention (Psychology)
The original version of our PPM program was modified to optimize positions of molecules in the lipid bilayer with the new solvation model. The computation requires only energy functions and parameters described in equations (142) and Tables S1, S3, S4. A solute molecule was considered as a rigid body whose spatial position was defined by three independent variables: two rotation angles and one translation along the bilayer normal (φ, τ and d, respectively). Transfer energy (equation 19) was optimized by combining grid scan and Davidon-Fletcher-Powell method for local energy minimization. Derivatives of transfer energy with respect to rigid body variables of the molecule were analytically calculated, as described previously22 (link). Derivatives of energy with respect to z were calculated as finite differences with step of 0.01 Å. The hydrophobic thickness of TM proteins was optimized by grid scan for location of the hydrocarbon boundary (ZHDC in eq. 2) with step of 0.05 Å. All other peaks of the lipid and water distributions were shifted accordingly during the optimization to remain at the same distance from the hydrocarbon boundary as in DOPC.
The program uses as input only a set of coordinate files in the PDB format. Unlike the previous version, it allows an automatic determination of transmembrane secondary structures without using any external software. The dipole moments and standard pKa values of different groups are included in the library of amino acid residues or directly in the PDB files for small molecules.
Publication 2011
1,2-oleoylphosphatidylcholine Amino Acids cDNA Library derivatives Energy Transfer Human Body Hydrocarbons Lipid Bilayers Lipids Muscle Rigidity Proteins Radionuclide Imaging

Most recents protocols related to «Hydrocarbons»

Not available on PMC !

Example 1

A renewable paraffinic product was produced by heavily cracking hydrodeoxygenation and isomerisation of feedstock mixture of vegetable and animal fat origin. This product was analysed using various analysis methods (Table 2).

TABLE 2
Analysed renewable paraffinic product.
AnalysisMethodUnitValue
Freezing pointIP529° C. −42.0
DensityASTM kg/m3753.0
D4052
Weighted average NM49012.0
carbon number
% carbon number 14-17NM490wt-%30.5
T10 (° C.) cut-off temperatureASTM D86° C. 168.5
T90 (° C.) cut-off temperatureASTM D86° C. 245.5
Final boiling pointASTM D86° C. 256.0

The analysed product in Table 2 fulfils the freezing point of jet fuel specification, but the freezing point is not exceptionally low.

Example 4

Another renewable paraffinic product produced by hydrodeoxygenation and isomerisation of another feedstock mixture of vegetable and animal fat origin is further directed to a fractionation unit. In the fractionation unit, the renewable paraffinic product is divided into two fractions. Lighter of the fractions containing 80 wt-% of the original renewable paraffinic product is re-analysed using various analysis methods (Table 5).

TABLE 5
Analysed renewable paraffinic product.
AnalysisMethodUnitValue
Freezing pointIP529° C.−50.9
DensityASTM kg/m3770.1
D4052
Weighted average NM49014.7
carbon number
% carbon number 14-17NM490wt-%73.6
T10 (° C.) cut-off temperatureASTM D86° C.191.9
T90 (° C.) cut-off temperatureASTM D86° C.276.6
Final boiling pointASTM D86° C.283.1

This product also fulfils all requirements of a high-quality renewable aviation fuels. From the analysis results it can be seen that despite the fact that the density of the paraffinic composition is over 768 kg/m3 (measured 770.1 kg/m3) the freezing point (measured −50.9° C.) is significantly lower than the freezing point of the product of comparative example 1.

It will be obvious to a person skilled in the art that, as the technology advances, the inventive concept can be implemented in various ways. The invention and its embodiments are not limited to the examples described above but may vary within the scope of the claims.

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Patent 2024
Animals Carbon-14 Carbon-17 Fractionation, Chemical Hydrocarbons jet fuel A Light Paraffin Vegetables Vision

Example 3

The ratio of the nanoparticles to the surface-active agent is an important factor as it controls the zeta potential of the nanoparticles and the time scale of the aggregation process. For zeta potential higher than ±30, the aggregation time scale is extremely long and may be infinite. As the zeta potential get s closer to the zero, the time scale of aggregations decreased significantly and optimally instantaneous at the zero.

FIG. 14 shows the gelation time of IL13, AB13, and NaOleate with Alu C and A-200. As shown, the gelation time can be controlled through these different combinations of formulations. The gelation is varying from instantaneous to 24 hrs. FIG. 15 shows the gelation time of IL22, AB22, and SDBS with Alu C and A-200. The gelation time is even extended to 35 hrs.

This wide range of gelation times may be made use of in different applications when these materials are emplaced in a porous medium, particularly when used in subterranean formations to assist in hydrocarbon recovery techniques. For example, materials with relatively long gelation times may be used post-CHOPS reservoirs to plug the wormholes. While materials with relatively short gelation times may be used for near-wellbore applications, such as water shutoff or acid diversion.

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Patent 2024
Acids Anabolism DDIT3 protein, human Hydrocarbons IL22 protein, human Interleukin-13 Surface-Active Agents
Not available on PMC !

Example 107

[Figure (not displayed)]

Compound 135. The mixture of succinimidyl ester 129 (4.6 mg, 0.0068 mmol), DIEA (24 μL, 0.0138 mmol) and 1-hexadecylamine (21 mg, 0.0087 mmol) in DMF (1 mL) and CHCl3 (2 mL) was stirred for 30 min, then diluted with chloroform (80 mL), washed with water (4×40 mL), brine 40 (mL), filtered through paper filter and evaporated. The residue was purified by chromatography on silica gel column (0.5×8 cm, packed with CHCl3/MeOH/AcOH/H2O (20:5:5:1)), eluant: CHCl3/MeOH/AcOH/H2O (20:5:5:1) to give amide 135 (4 mg, 73%) as a purple gum.

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Patent 2024
Amides Anabolism brine Chloroform Chromatography Esters hexadecylamine Hydrocarbons N,N-diisopropylethylamine Silica Gel
Not available on PMC !

Example 1

An Arab light crude oil with an API gravity of 33.0 and a sulfur content of 1.6 wt. % was fractionated in a distillation column to form a light stream and a heavy stream. Properties of the feed crude oil stream and the resulting fractions (based on their percent composition in the crude oil fractions) are given in Table 1 below.

TABLE 1
Stream NameBoiling RangeNi (ppm)V (ppm)S (wt. %)N (ppm)
Hydrocarbon3.414.521.6444
Feed
Light StreamLess than<1<10.213
370° C.
Heavy StreamGreater than 4.414.21.4431
370° C.

Details of the un-hydrotreated heavy stream are shown below in Table 2, where the heavy stream is designated EX-1(A).

The same Arab light crude oil used in Example 1 was directly cracked in the same cracking reactor and under the same conditions as was used in Example 3(A), results are designated CE-1. Specifically, the temperature was 675° and the TOS was 75 seconds.

TABLE 4
3(A)3(B)3 (Combined)CE-1
(wt. %)(wt. %)(wt. %)(wt. %)
Dry Gas9.876.438.0610.80
Light Olefins39.1151.6743.4634.89
Ethylene11.8210.0610.6910.41
Propylene18.3425.7621.0516.51
Butylene8.9615.8411.727.96
Gasoline Range33.1224.6028.3824.21
Products
Coke4.926.615.5113.86
Conversion91.1494.4689.8687.38

As can be seen in Table 4, the combined yields of total light olefins from the present methods are significantly higher than the yields from the comparative methods. Further, each of examples 3(A), 3(B), and 3(Combined) show significantly decreased levels of coke formation relative to the comparative example CE-1.

Example 2

The heavy stream from Example 1 was hydrotreated in a three-stage hydrotreater. The reaction conditions were: a weighted average bed temperature of 400° C., a pressure of 150 bar, a liquid hourly space velocity (LHSV) of 0.5 h−1, an Hz/oil ratio 1200:1(v/v), an oil flowrate of 300 ml/h, and an H2 flowrate of 360 L/h.

The first stage of the hydrotreater used a KFR-22 catalyst from Albemarle Co. to accomplish hydro-demetallization (HDM). The second stage of the hydrotreater used a KFR-33 catalyst from Albemarle Co. to accomplish hydro-desulfurization (HDS). The third stage of the hydrotreater used a KFR-70 catalyst from Albemarle Co. to accomplish hydro-dearomatization (HDA). The first, second, and third stages were discrete beds placed atop one another in a single reaction zone. The heavy stream flowed downward to the first stage, then to the second stage, and then to the third stage. Properties of this hydrotreated heavy stream are shown in Table 2 below and are designated EX-2.

TABLE 2
EX-1(A)EX-2
Kinematic viscosity at 100° C. (mm2/s)6
Density (g/ml)0.9650.8402
Nitrogen (ppm)120868.5
Sulfur (wt. %)3.10.007
Ni (ppm)10<1
V (ppm)32<1
Aromatics68.625.6

The hydrotreated heavy stream from Example 2 was fed to the advanced cracking evaluation unit. A TOS of 75 seconds, a residence time of from 1 to 2 seconds, and a temperature of 645° C. was used. Characterization of the product is given in Table 5 below.

TABLE 5
CE-13(B)
Temp. ° C.645645
T.O.S.(s)7575
Steaming Cond.810° C. for 6 hours
CAT/OIL6.488.00
Conversion (%)82.7794.46
Yields (wt. %)
H2 (wt. %)0.600.93
C1 (wt. %)4.823.71
C2 (wt. %)2.741.79
C2═ (wt. %)8.0710.06
C3 (wt. %)2.262.25
C3═ (wt. %)17.1625.76
iC4 (wt. %)0.671.58
nC4 (wt. %)0.550.69
t2C4═ (wt. %)2.393.92
1C4═ (wt. %)1.672.78
iC4═ (wt. %)3.596.01
c2C4═ (wt.%)1.903.14
1,3-BD (wt. %)0.010.63
Total Gas (wt. %)46.4463.25
Gasoline (wt. %)18.0924.60
LCO (wt. %)9.843.95
HCO (wt. %)7.381.59
Coke (wt. %)18.246.61
Groups (wt. %)
H2—C2 (dry gas)16.2416.49
C3—C4 (LPG)30.1946.77
C2═−C4═ (Light34.7952.30
olefins)
C3═+C426.7142.24
C4═ (Butenes)9.5516.48
Molar Ratios
mol/mol)
C2═/C23.156.03
C3═/C37.9711.97
C4═/C48.067.52
iC4═/C40.380.36
iC4═/iC45.513.94

As can be seen in Table 5, utilizing a hydrotreated heavy stream as the feed to the catalytic reactor results in higher conversion; greater yield of C2, C3, and C4 olefins; greater yield of gasoline; and significantly decreased coke formation, among other advantages.

Example 3

The respective fractions of Arab light crude were cracked at the conditions described below. A catalyst with the composition shown in Table 3 below as used in all of the reactions.

TABLE 3
ComponentWeight %Notes
ZSM-520Phosphorus impregnated at 7.5 wt. %
P2O5 on zeolite
USY21Lanthanum impregnated at 2.5 wt. %
La2O3 on zeolite
Alumina8Pural SB from Sasol
Clay49Kaolin
Silica2Added as colloidal silica Ludox TM-40

An Advanced Cracking Evaluation (ACE) unit was used to simulate a commercial FCC process. The reaction was run two times with fresh catalyst to simulate two separate FCC reaction zones in parallel.

Prior to each experiment, the catalyst is loaded into the reactor and heated to the desired reaction temperature. N2 gas is fed through the feed injector from the bottom to keep catalyst particles fluidized. Once the catalyst bed temperature reaches within ±2° C. of the reaction temperature, the reaction can begin. Feed is then injected for a predetermined time (time-on-stream (TOS)). The desired catalyst-to-feed ratio is obtained by controlling the feed pump. The gaseous product is routed to the liquid receiver, where C5+ hydrocarbons are condensed and the remaining gases are routed to the gas receiver. After catalyst stripping is over, the reactor is heated to 700° C., and nitrogen was replaced with air to regenerate the catalyst. During regeneration, the released gas is routed to a CO2 analyzer. Coke yield is calculated from the flue gas flow rate and CO2 concentration. The above process was repeated for each of Examples 3(A) and 3(B). The weight ratio of catalyst to hydrocarbons was 8.

It should be understood that time-on-stream (TOS) is directly proportional to residence time.

The light stream from Example 1 was fed to the advanced cracking evaluation unit. A time-on-stream (TOS) of 75 seconds, a residence time of from 1 to 2 seconds, and a temperature of 675° C. was used.

The hydrotreated heavy stream from Example 2 was fed to the advanced cracking evaluation unit. A TOS of 75 seconds, a residence time of from 1 to 2 seconds, and a temperature of 645° C. was used. Characterization is shown in both Table 4 and Table 5.

The streams of Examples 3(A) and 3(B) were combined to form a single stream. The single stream simulates the output of processing a whole crude according to the methods of the present disclosure.

Example 3(Combined) is a weighted average of Examples 3(A) and 3(B). Example 3(A) represented 53 wt. % of Example 3(Combined). Example 3(B) represented 44 wt. % of Example 3 (Combined).

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Patent 2024
Adjustment Disorders Alkenes Arabs butylene Catalysis Clay Cocaine Distillation ethylene GAS6 protein, human Gravity Hutterite cerebroosteonephrodysplasia syndrome Hydrocarbons Kaolin Lanthanum Light Molar Neoplasm Metastasis Nitrogen Oxide, Aluminum Petroleum phosphoric anhydride Phosphorus Pressure propylene Regeneration Silicon Dioxide Simulate composite resin Sulfur Viscosity Vision Zeolites

Example 1

An Arab light crude oil with an API gravity of 33.0 and a sulfur content of 1.6 wt. % was fractionated in a distillation column to form a light stream and a heavy stream. Properties of the feed crude oil stream and the resulting fractions (based on their wt. % composition in the crude oil) are given in Table 1 below.

TABLE 1
Boiling Ni VS N
Stream NameRange(ppm)(ppm)(wt. %)(ppm)
Hydrocarbon4.414.21.6444
Feed
Light StreamLess than <1<10.8136
540° C.
Heavy StreamGreater than4.414.20.8308
540° C.

The same Arab light crude oil used in Example 3 was directly cracked in the same cracking reactor and under the same conditions as was used in Example 3.

TABLE 4
EX-3CE-1
Constituent(wt. %)(wt. %)
H20.680.72
C16.476.86
C23.103.23
C2 = (ethylene)10.8510.41
C31.671.65
C3 = (propylene)18.2016.51
iC40.460.42
nC40.410.56
t2C4 =2.221.93
1C4 =1.651.40
iC4 =3.573.09
c2C4 =1.791.54
1,3-BD1.110.99
Butenes9.227.96
Total Gas52.1749.31
Dry Gas10.2410.80
Total Light Olefins38.2734.89
Gasoline27.9224.21
LCO8.439.43
HCO2.043.20
Coke9.4413.86
Total Gas + Coke61.6163.17

As can be seen in Table 4, the yield of total light olefins from the inventive EX-3 is significantly higher than the yield of light olefins in the comparative CE-1. Additionally, EX-3 shows significantly lower coke formation than the comparative CE-1.

Example 2

The heavy stream from Example 1 was hydrotreated in a three-stage hydrotreater. The reaction conditions were: a weighted average bed temperature of 400° C., a pressure of 150 bar, a liquid hourly space velocity (LHSV) of 0.5 h−1, an H2/oil ratio 1200:1 (v/v), an oil flowrate of 300 ml/h, and an H2 flowrate of 360 L/h.

The first stage of the hydrotreater used a KFR-22 catalyst from Albemarle Co. to accomplish hydro-demetallization (HDM). The second stage of the hydrotreater used a KFR-33 catalyst from Albemarle Co. to accomplish hydro-desulfurization (HDS). The third stage of the hydrotreater used a KFR-70 catalyst from Albemarle Co. to accomplish hydro-dearomatization (HDA). The first, second, and third stages were discrete beds placed atop one another in a single reaction zone. The heavy stream flowed downward to the first stage, then to the second stage, and then to the third stage. Properties of this hydrotreated heavy stream are shown in Table 2 below.

TABLE 2
Kinematic viscosity at 100° C.67.6 mm2/s
Density at 60° C.0.9 g/cm3
Sulfur (wt. %)0.36
Ni (ppm)1
V (ppm)3
Fe (ppm)<1
Na (ppm)<10

Example 3

A catalyst with the composition shown in Table 3 below as used in all of the reactions.

TABLE 3
ComponentWeight %Notes
ZSM-520Phosphorus impregnated at 7.5 wt. % P2O5
on zeolite
USY21Lanthanum impregnated at 2.5 wt. % La2O3
on zeolite
Alumina8Pural SB from Sasol
Clay49Kaolin
Silica2Added as colloidal silica Ludox TM-40

An Advanced Cracking Evaluation (ACE) unit was used to simulate a down-flow FCC reaction zone with multiple inlet points. The ACE unit emulates commercial FCC process.

Prior to each experiment, the catalyst is loaded into the reactor and heated to the desired reaction temperature. N2 gas is fed through the feed injector from the bottom to keep catalyst particles fluidized. Once the catalyst bed temperature reaches within ±2° C. of the reaction temperature, the reaction can begin. Feed is then injected for a predetermined time (time-on-stream (TOS)). The desired catalyst-to-feed ratio is obtained by controlling the feed pump. The gaseous product is routed to the liquid receiver, where C5+ hydrocarbons are condensed and the remaining gases are routed to the gas receiver. After catalyst stripping is over, the reactor is heated to 700° C., and nitrogen was replaced with air to regenerate the catalyst. During regeneration, the released gas is routed to a CO2 analyzer. Coke yield is calculated from the flue gas flow rate and CO2 concentration. The above process was repeated for each of Examples 3(A) and 3(B).

The light stream from Example 1 was combined with the hydrotreated heavy stream from Example 2 to form a combined feed stream. The combined feed stream was fed to the ACE unit. A time-on-stream (TOS) of 75 seconds and a temperature of 675° C. was used. Fresh catalyst was steamed deactivated at 810° C. for 6 hours to resemble the equilibrium catalyst in the actual process. The steam deactivated catalyst was used in this reaction. It should be understood that TOS is directly proportional to residence time.

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Patent 2024
43-63 Adjustment Disorders Alkenes Arabs BD-38 butylene Catalysis Clay Cocaine Distillation ethylene Gravity Hydrocarbons Kaolin Lanthanum Light Neoplasm Metastasis Nitrogen Oxide, Aluminum Petroleum phosphoric anhydride Phosphorus Pressure propylene Regeneration Silicon Dioxide Steam Sulfur Viscosity Vision Zeolites

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The HP-5MS capillary column is a gas chromatography column designed for a wide range of applications. It features a 5% phenyl-methylpolysiloxane stationary phase and is suitable for the separation and analysis of a variety of organic compounds.
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The ESCALAB 250Xi is a high-performance X-ray photoelectron spectroscopy (XPS) system designed for surface analysis. It provides precise and reliable data for the characterization of materials at the nanoscale level.
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The GCMS-QP2010 is a gas chromatograph-mass spectrometer system manufactured by Shimadzu. It is designed for the analysis and identification of chemical compounds in complex samples. The system combines a high-performance gas chromatograph with a sensitive quadrupole mass spectrometer to provide accurate and reliable analytical results.
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DMSO is a versatile organic solvent commonly used in laboratory settings. It has a high boiling point, low viscosity, and the ability to dissolve a wide range of polar and non-polar compounds. DMSO's core function is as a solvent, allowing for the effective dissolution and handling of various chemical substances during research and experimentation.
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The DB-5 capillary column is a widely used gas chromatography (GC) column designed for the separation and analysis of a wide range of organic compounds. It features a nonpolar stationary phase, making it suitable for the separation of a variety of analytes. The column is constructed with a fused silica capillary and a bonded phenyl-methyl siloxane stationary phase. This combination provides efficient separation and reliable performance for a diverse range of applications.
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Anhydrous sodium sulfate is a chemical compound with the formula Na2SO4. It is a white crystalline solid that is commonly used as a drying agent in organic synthesis and other laboratory applications. Anhydrous sodium sulfate is highly hygroscopic, meaning it readily absorbs water from the environment, making it useful for removing traces of water from organic solvents and other materials.
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The HP-5MS column is a fused silica capillary column used for gas chromatography. It is designed for the separation and analysis of a wide range of organic compounds.
Sourced in United States, Japan
The HP-5 capillary column is a gas chromatography column designed for the separation and analysis of a wide range of organic compounds. It features a fused silica capillary with a 5% phenyl-methylpolysiloxane stationary phase, providing efficient separation and good thermal stability.

More about "Hydrocarbons"

Hydrocarbons are a fundamental class of organic compounds composed solely of carbon and hydrogen atoms.
They are the simplest organic molecules and serve as the building blocks for a wide range of fuels, chemicals, and materials essential to modern industry and society.
Hydrocarbons can exist in various forms, including alkanes, alkenes, alkynes, and aromatic compounds, each with unique structural and chemical properties.
These versatile molecules play a crucial role in the energy, petrochemical, and pharmaceutical industries, as well as in many everyday products.
Researchers and scientists continually explore the production, properties, and applications of hydrocarbons to advance our understanding and utilization of this vital group of compounds.
Alkanes, such as N-hexadecane and Hexadecane, are saturated hydrocarbons that find use in fuels, lubricants, and solvents.
Analytical techniques like GC-MS, using columns like HP-5MS, ESCALAB 250Xi, and GCMS-QP2010, are often employed to study and characterize hydrocarbon samples.
Solvents like DMSO can be used in hydrocarbon-related research and extraction processes.
Hydrocarbon-based polymers and derivatives are widely used in the production of plastics, rubbers, and other materials.
The comprehensive knowledge of hydrocarbons and their properties is essential for unlocking new discoveries and innovations in various industries.