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Cetyl Palmitate, also known as synthetic spermaceti, is an ester of palmitic acid obtained through the reaction of cetyl alcohol and palmitic acid. It is a white to almost white crystalline powder and is widely used in the cosmetic and pharmaceutical industries due to its various beneficial properties.

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  • 540-10-3 Structure
  • Basic information

    1. Product Name: CETYL PALMITATE
    2. Synonyms: SPERMACETI;PALMATIC ACID N-HEXADECYL ESTER;SperMwax;Cetyl Palmitate (50 mg);n-Hexadecyl palMitate, 98% 25GR;n-Hexadecyl palMitate, 98% 5GR;Cetyl Palmitate Palmitic Acid Hexadecyl Ester;PalMityl palMitate, 95+%
    3. CAS NO:540-10-3
    4. Molecular Formula: C32H64O2
    5. Molecular Weight: 480.85
    6. EINECS: 208-736-6
    7. Product Categories: Aliphatics;Fatty Acid Derivatives & Lipids;Glycerols
    8. Mol File: 540-10-3.mol
  • Chemical Properties

    1. Melting Point: 55-56 °C(lit.)
    2. Boiling Point: 360 °C
    3. Flash Point: 269.8 °C
    4. Appearance: White to almost white/Crystalline Powder
    5. Density: d20 0.989
    6. Refractive Index: 1.4429 (589.3 nm 60℃)
    7. Storage Temp.: 2-8°C
    8. Solubility: Soluble in hot acetone.
    9. Merck: 14,2031
    10. CAS DataBase Reference: CETYL PALMITATE(CAS DataBase Reference)
    11. NIST Chemistry Reference: CETYL PALMITATE(540-10-3)
    12. EPA Substance Registry System: CETYL PALMITATE(540-10-3)
  • Safety Data

    1. Hazard Codes: N/A
    2. Statements: N/A
    3. Safety Statements: 24/25
    4. WGK Germany: -
    5. RTECS: RT4750000
    6. TSCA: Yes
    7. HazardClass: N/A
    8. PackingGroup: N/A
    9. Hazardous Substances Data: 540-10-3(Hazardous Substances Data)

540-10-3 Usage

Uses

Used in Cosmetic and Personal Care Industry:
Cetyl Palmitate is used as an emollient, masking agent, and skin conditioning agent for its ability to improve skin texture and provide a smooth, soft feel. It also acts as a glosser and thickener for creams, enhancing emulsion texture and stability, and giving structure to cosmetic sticks.
Used in Pharmaceutical Industry:
Cetyl Palmitate serves as an ingredient in many cosmetic preparations and is also utilized in pharmaceutical secondary standards for application in quality control. It provides a convenient and cost-effective alternative to the preparation of in-house working standards for pharmaceutical laboratories and manufacturers.

Flammability and Explosibility

Notclassified

Check Digit Verification of cas no

The CAS Registry Mumber 540-10-3 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 5,4 and 0 respectively; the second part has 2 digits, 1 and 0 respectively.
Calculate Digit Verification of CAS Registry Number 540-10:
(5*5)+(4*4)+(3*0)+(2*1)+(1*0)=43
43 % 10 = 3
So 540-10-3 is a valid CAS Registry Number.
InChI:InChI=1S/C32H64O2/c1-3-5-7-9-11-13-15-17-19-21-23-25-27-29-31-34-32(33)30-28-26-24-22-20-18-16-14-12-10-8-6-4-2/h3-31H2,1-2H3

540-10-3 Well-known Company Product Price

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  • Alfa Aesar

  • (H59283)  Palmityl palmitate, 96%   

  • 540-10-3

  • 1g

  • 572.0CNY

  • Detail
  • Alfa Aesar

  • (H59283)  Palmityl palmitate, 96%   

  • 540-10-3

  • 5g

  • 2040.0CNY

  • Detail
  • Sigma-Aldrich

  • (PHR1166)  Cetyl Palmitate  pharmaceutical secondary standard; traceable to USP and PhEur

  • 540-10-3

  • PHR1166-1G

  • 732.19CNY

  • Detail
  • Sigma-Aldrich

  • (Y0000073)  Cetyl palmitate 15  European Pharmacopoeia (EP) Reference Standard

  • 540-10-3

  • Y0000073

  • 1,880.19CNY

  • Detail
  • Sigma-Aldrich

  • (Y0000074)  Cetyl palmitate 95  European Pharmacopoeia (EP) Reference Standard

  • 540-10-3

  • Y0000074

  • 1,880.19CNY

  • Detail
  • USP

  • (1103105)  Cetyl palmitate  United States Pharmacopeia (USP) Reference Standard

  • 540-10-3

  • 1103105-50MG

  • 4,647.24CNY

  • Detail

540-10-3SDS

SAFETY DATA SHEETS

According to Globally Harmonized System of Classification and Labelling of Chemicals (GHS) - Sixth revised edition

Version: 1.0

Creation Date: Aug 12, 2017

Revision Date: Aug 12, 2017

1.Identification

1.1 GHS Product identifier

Product name palmityl palmitate

1.2 Other means of identification

Product number -
Other names Hexadecyl hexadecanoate

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only.
Uses advised against no data available

1.4 Supplier's details

1.5 Emergency phone number

Emergency phone number -
Service hours Monday to Friday, 9am-5pm (Standard time zone: UTC/GMT +8 hours).

More Details:540-10-3 SDS

540-10-3Synthetic route

1-Hexadecanol
36653-82-4

1-Hexadecanol

1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
With zirconium(IV) oxychloride In 1,3,5-trimethyl-benzene at 162℃; for 24h;99.5%
hafnium(IV) oxychloride In 1,3,5-trimethyl-benzene at 162℃; for 24h;98.7%
With choline chloride; zinc(II) chloride at 110℃; for 10h;97%
1-Hexadecanol
36653-82-4

1-Hexadecanol

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
With sodium bromate; sulfuric acid; sodium bromide In water at 20℃; for 24h;99%
With [bis(2-methylallyl)cycloocta-1,5-diene]ruthenium(II); (2-((2-(diphenylphosphanyl)ethyl)(quinolin-2-ylmethyl)amino)ethyl)diphenylphosphine oxide; potassium tert-butylate In n-heptane at 100℃; for 16h;86%
1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

A

1-Hexadecanol
36653-82-4

1-Hexadecanol

B

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
With trimethylamine borane In xylene for 9h; Heating;A 22%
B 61%
With hydrogen; zirconium(IV) oxide In dodecane at 20 - 260℃; under 9000.9 Torr; Kinetics; Autoclave;
1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
With hydrogen In neat (no solvent) at 20 - 200℃; under 6000.6 Torr; for 24h; Autoclave; High pressure;55%
With copper chromite; hydrogen at 360℃;
1-iodohexadecane
544-77-4

1-iodohexadecane

silver palmitate
3508-01-8

silver palmitate

cetyl palmitate
540-10-3

cetyl palmitate

1-Hexadecanol
36653-82-4

1-Hexadecanol

n-hexadecanoyl chloride
112-67-4

n-hexadecanoyl chloride

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
With quinoline; chloroform anfangs unter Kuehlung, dann bei Zimmertemperatur;
With diethyl ether; magnesium
With pyridine
In pyridine; chloroform
n-hexadecanoyl chloride
112-67-4

n-hexadecanoyl chloride

catyl alcohol

catyl alcohol

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
at 180℃;
1-Hexadecanol
36653-82-4

1-Hexadecanol

n-tetradecanoic acid
544-63-8

n-tetradecanoic acid

1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

A

tetradecanoic acid hexadecyl ester
2599-01-1

tetradecanoic acid hexadecyl ester

B

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
With phosphoric acid In hexane; water for 8.5h; Product distribution / selectivity; Heating / reflux;
With phosphoric acid In n-heptane; water for 18h; Product distribution / selectivity; Heating / reflux;
With phosphoric acid In water; toluene at 92℃; for 38.5h; Product distribution / selectivity; Heating / reflux;
With phosphoric acid In water; xylene at 105℃; for 1h; Product distribution / selectivity;
With phosphoric acid In water at 95℃; for 0.5h; Product distribution / selectivity;
1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

A

pentadecane
629-62-9

pentadecane

B

Hexadecane
544-76-3

Hexadecane

C

1-Hexadecanol
36653-82-4

1-Hexadecanol

D

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
With hydrogen In dodecane at 20 - 260℃; under 9000.9 Torr; Kinetics; Autoclave;
1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

A

pentadecane
629-62-9

pentadecane

B

1-Hexadecanol
36653-82-4

1-Hexadecanol

C

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
With hydrogen In dodecane at 20 - 260℃; under 9000.9 Torr; Kinetics; Autoclave;
With hydrogen In dodecane at 280℃; under 39003.9 Torr; for 6h; Catalytic behavior; Kinetics; Time;
hexadecanoic acid methyl ester
112-39-0

hexadecanoic acid methyl ester

A

1-Hexadecanol
36653-82-4

1-Hexadecanol

B

n-hexadecylaldehyde
629-80-1

n-hexadecylaldehyde

C

palmitone
502-73-8

palmitone

D

cetyl palmitate
540-10-3

cetyl palmitate

E

1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

Conditions
ConditionsYield
With hydrogen; zirconium(IV) oxide at 700℃; under 60006 Torr; Kinetics; Reagent/catalyst; Temperature; Pressure; Calcination;
hexadecanoic acid methyl ester
112-39-0

hexadecanoic acid methyl ester

A

pentadecane
629-62-9

pentadecane

B

methane
34557-54-5

methane

C

Hexadecane
544-76-3

Hexadecane

D

hexadecan-2-ol
14852-31-4

hexadecan-2-ol

E

1-Hexadecanol
36653-82-4

1-Hexadecanol

F

n-hexadecylaldehyde
629-80-1

n-hexadecylaldehyde

G

cetyl palmitate
540-10-3

cetyl palmitate

H

carbon dioxide
124-38-9

carbon dioxide

I

carbon monoxide
201230-82-2

carbon monoxide

J

1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

Conditions
ConditionsYield
With hydrogen In dodecane at 290℃; under 22502.3 Torr;
hexadecanoic acid methyl ester
112-39-0

hexadecanoic acid methyl ester

A

pentadecane
629-62-9

pentadecane

B

methane
34557-54-5

methane

C

Hexadecane
544-76-3

Hexadecane

D

hexadecan-2-ol
14852-31-4

hexadecan-2-ol

E

1-Hexadecanol
36653-82-4

1-Hexadecanol

F

n-hexadecylaldehyde
629-80-1

n-hexadecylaldehyde

G

cetyl palmitate
540-10-3

cetyl palmitate

H

carbon monoxide
201230-82-2

carbon monoxide

I

1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

Conditions
ConditionsYield
With hydrogen In dodecane at 290℃; under 22502.3 Torr;
1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

A

pentadecane
629-62-9

pentadecane

B

Hexadecane
544-76-3

Hexadecane

C

1-Hexadecanol
36653-82-4

1-Hexadecanol

D

n-hexadecylaldehyde
629-80-1

n-hexadecylaldehyde

E

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
With hydrogen In dodecane at 280℃; under 39003.9 Torr; for 6h; Kinetics;
1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

A

Hexadecane
544-76-3

Hexadecane

B

1-Hexadecanol
36653-82-4

1-Hexadecanol

C

n-hexadecylaldehyde
629-80-1

n-hexadecylaldehyde

D

cetyl palmitate
540-10-3

cetyl palmitate

Conditions
ConditionsYield
With hydrogen In dodecane at 280℃; under 39003.9 Torr; for 6h; Kinetics;
cetyl palmitate
540-10-3

cetyl palmitate

O-hexadecyl hexadecanethiono ester

O-hexadecyl hexadecanethiono ester

Conditions
ConditionsYield
With Lawessons reagent In 5,5-dimethyl-1,3-cyclohexadiene Reflux;58%
cetyl palmitate
540-10-3

cetyl palmitate

n-hexadecylaldehyde
629-80-1

n-hexadecylaldehyde

Conditions
ConditionsYield
With dimethylsulfide borane complex; pyridinium chlorochromate 1) THF, reflux, 1 h, 2.) CH2Cl2, reflux, 1 h; Yield given. Multistep reaction;
cetyl palmitate
540-10-3

cetyl palmitate

<1-14C>n-hexadecanol palmitate

<1-14C>n-hexadecanol palmitate

Conditions
ConditionsYield
With 1-(14)C cetyl alcohol In acetone at 40℃; for 1h; transesterification with enzyme from Sinapis alba L.;
cetyl palmitate
540-10-3

cetyl palmitate

<4-14C>cholesteryl palmitate

<4-14C>cholesteryl palmitate

Conditions
ConditionsYield
With [14C]-Cholesterol In acetone at 40℃; for 1h; transesterification with enzyme from Sinapis alba L.; influence of incubation time and <1-14C>n-hexadecanol concentration on ester formation; double pH optima: 6.4, 8.4;
cetyl palmitate
540-10-3

cetyl palmitate

α-particle/s

α-particle/s

A

hydrogen

hydrogen

B

carbon oxides

carbon oxides

C

hydrocarbons

hydrocarbons

Conditions
ConditionsYield
Irradiation;
monoglyceryl stearate

monoglyceryl stearate

cetyl palmitate
540-10-3

cetyl palmitate

A

monocetylphosphoric ester potassium salt

monocetylphosphoric ester potassium salt

B

acrylic acid
79-10-7

acrylic acid

540-10-3Relevant articles and documents

Esterification of cetyl alcohol with palmitic acid over WO3/Zr-SBA-15 and Zr-SBA-15 catalysts

Mutlu, Vahide Nuran,Yilmaz, Selahattin

, p. 194 - 200 (2016)

Tungsten loaded and Zr incorporated SBA-15 catalysts (WO3/Zr-SBA-15 and Zr-SBA-15) were developed for esterification of cetyl alcohol and palmitic acid. The influence of the Zr content, tungsten loading amount, calcination temperature, feed composition and catalyst amount has been studied. Higher tungsten loading decreased the acidity due to formation of WO3 crystals whereas calcination temperature enhanced the acidity by favoring the dispersion of WOx species. Activities of the catalyst changed depending on their amount of Br?nsted sites and total number of acid sites. Zr-SBA-15 catalyst which had the highest amount of Br?nsted acid sites gave maximum cetyl palmitate yield (63.1%). This catalyst retained its activity up to 3 reuse cycles without significant loss of activity.

Ni-Based heterogeneous catalysts for the transformation of fatty acids into higher yields of O-free hydrocarbons

Aburto, Jorge,Gómez-Pérez, María Teresa,Gómora-Herrera, Diana,Valencia, Diego,Zenteno, Citlalli

, p. 3470 - 3480 (2020/06/25)

A series of novel catalytic materials were synthesized by changing the chemical compounds in the impregnation solutions. A rigid, aromatic and bidentate molecule 1,10-phenanthroline (PhN) was used as a ligand to bind Ni2+species prior to impregnation into a mesoporous KIT-5 support. Thein situsynthesized coordination compounds were impregnated into KIT-5 and the resulting materials exhibited better dispersion of metal species, being the best at a molar ratio Ni?:?PhN = 1?:?1. The materials were tested in the hydrodeoxygenation (HDO) of palmitic acid. We found that highly active and stable catalysts were obtained when using PhN as a chelating agent in the impregnation solution. The selectivity of these materials is remarkable since only O-free molecules were detected in the HDO products. Therefore, Ni-PhN complexes in combination with mesoporous SiO2can be further exploited for the catalytic transformation of biomass feedstocks.

Paving the way towards green catalytic materials for green fuels: Impact of chemical species on Mo-based catalysts for hydrodeoxygenation

Valencia, Diego,Díaz-García, Leonardo,Ramírez-Verduzco, Luis Felipe,Qamar, Amir,Moewes, Alexander,Aburto, Jorge

, p. 18292 - 18301 (2019/07/03)

A series of Mo-based catalysts were synthesized by tuning the sulfidation temperature to produce mixtures of MoO3 and MoS2 as active phases for the hydrodeoxygenation (HDO) of palmitic acid. Differences in the oxidation states of Mo, and the chemical species present in the catalytic materials were determined by spectroscopic techniques. Palmitic acid was used as a fatty-acid model compound to test the performance of these catalysts. The catalytic performance was related to different chemical species formed within the materials. Sulfidation of these otherwise inactive catalysts significantly increased their performance. The catalytic activity remains optimal between the sulfidation temperatures of 100 °C and 200 °C, whereas the most active catalyst was obtained at 200 °C. The catalytic performance decreased significantly at 400 °C due to a higher proportion of sulfides formed in the materials. Furthermore, the relative proportion of MoO3 to MoS2 is essential to form highly active materials to produce O-free hydrocarbons from biomass feedstock. The transition from MoS2 to MoO3 reveals the importance of Mo-S and Mo-O catalytically active species needed for the HDO process and hence for biomass transformation. We conclude that transitioning from MoS2 to MoO3 catalysts is a step in the right direction to produce green fuels.

PRODUCTION METHOD OF ESTER COMPOUND

-

Paragraph 0030; 0032; 0033; 0035-0047, (2019/10/01)

PROBLEM TO BE SOLVED: To produce an ester compound at a high conversion even under mild reaction conditions. SOLUTION: A production method of an ester compound includes a reaction step for reacting a carboxylic acid of 8-22 carbons and an alcohol of 8-22 carbons at a temperature of 50-100°C in an ionic liquid composed of a phosphonium cation or an imidazolium cation and a trifluoromethanesulfonic acid anion or a bis (trifluoromethanesulfonyl) imide anion to obtain an ester compound in a liquid phase different from an ionic liquid phase. SELECTED DRAWING: None COPYRIGHT: (C)2019,JPOandINPIT

Aldehyde effect and ligand discovery in Ru-catalyzed dehydrogenative cross-coupling of alcohols to esters

Jiang, Xiaolin,Zhang, Jiahui,Zhao, Dongmei,Li, Yuehui

, p. 2797 - 2800 (2019/03/27)

The presence of different aldehydes is found to have a significant influence on the catalytic performance when using PN(H)P type ligands for dehydrogenation of alcohols. Accordingly, hybrid multi-dentate ligands were discovered based on an oxygen-transfer alkylation of PNP ligands by aldehydes. The relevant Ru-PNN(PO) system provided the desired unsymmetrical esters in good yields via acceptorless dehydrogenation of alcohols. Hydrogen bonding interactions between the phosphine oxide moieties and alcohol substrates likely assisted the observed high chemoselectivity.

Oxidative esterification of primary alcohols at room temperature under aqueous medium

Reddy, N. Naresh Kumar,Ravi, Chitrakar,Adimurthy, Subbarayappa

, p. 1663 - 1670 (2018/06/15)

Oxidative esterification of aliphatic primary alcohols with bromide and bromate couple in aqueous acidic medium at room temperature is reported with a wide range of substrate scope for both aliphatic and cyclic alcohols and obtained excellent yields of products.

Effect of precursor on the catalytic properties of Ni2P/SiO2 in methyl palmitate hydrodeoxygenation

Shamanaev, Ivan V.,Deliy, Irina V.,Aleksandrov, Pavel V.,Gerasimov, Evgeny Yu.,Pakharukova, Vera P.,Kodenev, Evgeny G.,Ayupov, Artem B.,Andreev, Andrey S.,Lapina, Olga B.,Bukhtiyarova, Galina A.

, p. 30372 - 30383 (2017/02/23)

The effect of phosphorus precursor on the physicochemical and catalytic properties of silica-supported nickel phosphide catalysts in the hydrodeoxygenation (HDO) of aliphatic model compound methyl palmitate (C15H31COOCH3) has been considered. Nickel aceta

Hydrodeoxygenation (HDO) of methyl palmitate over bifunctional Rh/ZrO2 catalyst: Insights into reaction mechanism via kinetic modeling

Bie, Yuwei,Lehtonen, Juha,Kanervo, Jaana

, p. 183 - 190 (2016/09/13)

Hydrodeoxygenation (HDO) of triglycerides into hydrocarbons is a novel catalytic process for the production of green biofuels. In this work, the HDO reaction mechanism over Rh/ZrO2 catalyst was studied by selecting methyl palmitate as a model compound. HDO of methyl palmitate proceeded initially via the hydrogenolysis into palmitic acid intermediate, followed by sequential hydrogenation-decarbonylation reaction into pentadecane via aldehyde intermediate. Bifunctional mechanism of the Rh/ZrO2 catalyst is advocated for the HDO process, in which both Rh sites and oxygen vacancy sites on ZrO2 synergistically contribute to the catalysis. The interface between Rh nanoparticle and support was proposed to host the most active sites. Based on our earlier work, a surface reaction mechanism was proposed and slightly modified to develop a set of mechanistic kinetic models. The mechanistic model consisting of two distinct types of adsorption sites for oxygenated components and H2, gave a good fitting to the kinetic data over a broad range of reaction conditions and conversion levels.

Unprecedented reductive esterification of carboxylic acids under hydrogen by reusable heterogeneous platinum catalysts

Touchy, Abeda S.,Kon, Kenichi,Onodera, Wataru,Shimizu, Ken-Ichi

, p. 1499 - 1506 (2015/05/19)

Supported metal catalysts have been tested for an unprecedented reductive dimerization of carboxylic acids to esters under 8 bar hydrogen in solvent-free conditions. Among various metal-loaded tin oxide catalysts, platinum-loaded tin dioxide (Pt/SnO2) shows the highest ester yield for the reaction of dodecanoic acid. Among Pt catalysts on various supports, Lewis acidic oxides, especially SnO2, show high activity. The most active catalyst, 5 wt% Pt/SnO2 reduced at 100°C, is effective for the reductive esterification of various carboxylic acids, and the catalyst is reusable for nine cycles, demonstrating the first successful example for the title reaction. Infrared (IR) studies of a model compound (formic acid) on some metal oxides indicate a strong Lewis acid-base interaction between SnO2 and the carbonyl oxygen. For Pt/SnO2 catalysts with different Pt particle sizes, the activity increases with decreasing size of Pt metal. A cooperative catalysis of the Pt metal nanoparticles and the Sn4+ Lewis acid sites is proposed.

Manipulating catalytic pathways: Deoxygenation of palmitic acid on multifunctional catalysts

Peng, Baoxiang,Zhao, Chen,Kasakov, Stanislav,Foraita, Sebastian,Lercher, Johannes A.

, p. 4732 - 4741 (2013/05/22)

The mechanism of the catalytic reduction of palmitic acid to n-pentadecane at 260 °C in the presence of hydrogen over catalysts combining multiple functions has been explored. The reaction involves rate-determining reduction of the carboxylic group of palmitic acid to give hexadecanal, which is catalyzed either solely by Ni or synergistically by Ni and the ZrO2 support. The latter route involves adsorption of the carboxylic acid group at an oxygen vacancy of ZrO2 and abstraction of the α-H with elimination of O to produce the ketene, which is in turn hydrogenated to the aldehyde over Ni sites. The aldehyde is subsequently decarbonylated to n-pentadecane on Ni. The rate of deoxygenation of palmitic acid is higher on Ni/ZrO2 than that on Ni/SiO2 or Ni/Al2O3, but is slower than that on H-zeolite-supported Ni. As the partial pressure of H2 is decreased, the overall deoxygenation rate decreases. In the absence of H 2, ketonization catalyzed by ZrO2 is the dominant reaction. Pd/C favors direct decarboxylation (-CO2), while Pt/C and Raney Ni catalyze the direct decarbonylation pathway (-CO). The rate of deoxygenation of palmitic acid (in units of mmol moltotal metal -1 h-1) decreases in the sequence r (Pt black)≈r(Pd black)>r(Raney Ni) in the absence of H2. In situ IR spectroscopy unequivocally shows the presence of adsorbed ketene (Ci?£34;Ci?£34;O) on the surface of ZrO2 during the reaction with palmitic acid at 260 °C in the presence or absence of H2. Biomass to biofuels: The conversion of palmitic acid to n-pentadecane over ZrO2 mainly proceeds by hydrogenation of the carboxylic acid group to give hexadecanal (rate-determining step), which is catalyzed either solely by Ni sites or synergistically by Ni sites and sites on the ZrO2 support (see scheme). In the absence of H2, ketonization is the dominant reaction catalyzed by ZrO 2. Copyright

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