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CAS

  • or
1-Hydroxyoctadecane, also known as Octadecan-1-ol or 1-Octadecanol, is a long-chain primary fatty alcohol consisting of a hydroxy function at the first carbon of an unbranched saturated chain of 18 carbon atoms. It is a plant, human, and algal metabolite and is derived from a hydride of an octadecane. It occurs naturally in sperm whale oil and has been isolated from the hyperthermophilic bacterium Pyrococcus furiosus. 1-Hydroxyoctadecane is used in various industries due to its unique properties, such as being a saturated alcohol of high purity, soluble in alcohol, acetone, and ether, and insoluble in water.

112-92-5

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112-92-5 Usage

Uses

Used in Cosmetics:
1-Hydroxyoctadecane is used as a surfactant for effective hydration in cosmetics, particularly for hands and face. It is a component of pheohydrane, a complex of micro algae Chlorella Vulgaris and hydrolysed algin in a sea water base.
Used in Pharmaceutical Dispensing:
1-Hydroxyoctadecane is used as a substitute for cetyl alcohol in pharmaceutical dispensing, due to its high purity and similar properties.
Used in Cosmetic Creams:
It is utilized in the formulation of cosmetic creams for its emulsifying and moisturizing properties.
Used in Textile Industry:
1-Hydroxyoctadecane is used in the textile industry as an oil and finish, providing lubrication and improving the texture of fabrics.
Used as an Antifoam Agent:
It serves as an antifoam agent in various industrial applications, helping to control and prevent foam formation.
Used as a Lubricant:
1-Hydroxyoctadecane is used as a lubricant in the manufacturing of various products, reducing friction and wear.
Used as a Viscosity Agent:
It is employed as a viscosity agent to control the flow and consistency of different substances.
Used in Chemical Raw Material:
1-Hydroxyoctadecane is used as a chemical raw material in the production of alkyl amines, tertiary amines, ethoxylates, halides/mercaptans, and polymerization stabilizers.
Used in Emulsions Production:
It is a key component in the production of emulsions, which are essential in various industries, including cosmetics and pharmaceuticals.
Used in Microsphere Formulations:
1-Hydroxyoctadecane has been used to prepare microsphere formulations for compounds such as paclitaxel and indomethacin, enhancing their delivery and efficacy.
Used in Plant Epicuticular Wax Layer Research:
It has been used to model the plant epicuticular wax layer for investigations using differential scanning calorimetry and Fourier transform infrared spectroscopy.

Production Methods

Historically, stearyl alcohol was prepared from sperm whale oil but is now largely prepared synthetically by reduction of ethyl stearate with lithium aluminum hydride.

Synthesis Reference(s)

The Journal of Organic Chemistry, 49, p. 2438, 1984 DOI: 10.1021/jo00187a028Synthetic Communications, 12, p. 463, 1982 DOI: 10.1080/00397918208065953

Health Hazard

Mildly toxic by ingestion. Questionable carcinogen with experimental neoplastigenic data. A skin and eye irritant.

Fire Hazard

Flammable when exposed to heat or flame; can react with oxidizing materials. To fight fire, use foam, CO2, dry chemical. When heated to decomposition it emits acrid smoke and irritating fumes.

Flammability and Explosibility

Notclassified

Pharmaceutical Applications

1-Octadecanol is used in cosmetics and topical pharmaceutical creams and ointments as a stiffening agent. By increasing the viscosity of an emulsion, stearyl alcohol increases its stability. 1-Octadecanol also has some emollient and weak emulsifying properties, and is used to increase the water-holding capacity of ointments, e.g. petrolatum. In addition, 1-Octadecanol has been used in controlled-release tablets, suppositories, and microspheres.It has also been investigated for use as a transdermal penetration enhancer.

Safety

Stearyl alcohol is generally considered to be an innocuous, nontoxic material. However, adverse reactions to stearyl alcohol present in topical preparations have been reported. These include contact urticaria and hypersensitivity reactions, which are possibly due to impurities contained in stearyl alcohol rather than stearyl alcohol itself. The probable lethal oral human dose is greater than 15 g/kg. LD50 (rat, oral): 20 g/kg

storage

Stearyl alcohol is stable to acids and alkalis and does not usually become rancid. It should be stored in a well-closed container in a cool, dry place.

Purification Methods

Crystallise octadecanol from MeOH, or dry Et2O and *C6H6, then fractionally distil it in vacuo. Also purify it by column chromatography. Free it from cetyl alcohol by zone refining. [Beilstein 1 IV 1888.]

Incompatibilities

Incompatible with strong oxidizing agents and strong acids.

Regulatory Status

Included in the FDA Inactive Ingredients Database (oral tablets, rectal topical, and vaginal preparations). Included in nonparenteral medicines licensed in the UK. Included in the Canadian List of Acceptable Non-medicinal Ingredients.

Check Digit Verification of cas no

The CAS Registry Mumber 112-92-5 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 1,1 and 2 respectively; the second part has 2 digits, 9 and 2 respectively.
Calculate Digit Verification of CAS Registry Number 112-92:
(5*1)+(4*1)+(3*2)+(2*9)+(1*2)=35
35 % 10 = 5
So 112-92-5 is a valid CAS Registry Number.
InChI:InChI=1/C18H38O/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19/h19H,2-18H2,1H3

112-92-5 Well-known Company Product Price

  • Brand
  • (Code)Product description
  • CAS number
  • Packaging
  • Price
  • Detail
  • Alfa Aesar

  • (A12020)  1-Octadecanol, 97%   

  • 112-92-5

  • 250g

  • 171.0CNY

  • Detail
  • Alfa Aesar

  • (A12020)  1-Octadecanol, 97%   

  • 112-92-5

  • 500g

  • 205.0CNY

  • Detail
  • Alfa Aesar

  • (A12020)  1-Octadecanol, 97%   

  • 112-92-5

  • 2500g

  • 525.0CNY

  • Detail
  • Sigma-Aldrich

  • (PHR1115)    pharmaceutical secondary standard; traceable to USP and PhEur

  • 112-92-5

  • PHR1115-1G

  • 732.19CNY

  • Detail
  • Sigma-Aldrich

  • (S1350000)  Stearylalcohol  European Pharmacopoeia (EP) Reference Standard

  • 112-92-5

  • S1350000

  • 1,880.19CNY

  • Detail
  • USP

  • (1622000)  Stearylalcohol  United States Pharmacopeia (USP) Reference Standard

  • 112-92-5

  • 1622000-125MG

  • 3,720.60CNY

  • Detail
  • Aldrich

  • (O709)  1-Octadecanol  95%

  • 112-92-5

  • O709-1KG

  • 380.25CNY

  • Detail
  • Aldrich

  • (O709)  1-Octadecanol  95%

  • 112-92-5

  • O709-2KG

  • 1,334.97CNY

  • Detail
  • Aldrich

  • (258768)  1-Octadecanol  ReagentPlus®, 99%

  • 112-92-5

  • 258768-5G

  • 228.15CNY

  • Detail
  • Aldrich

  • (258768)  1-Octadecanol  ReagentPlus®, 99%

  • 112-92-5

  • 258768-100G

  • 460.98CNY

  • Detail
  • Sigma-Aldrich

  • (74723)  1-Octadecanol  Selectophore, ≥99.5%

  • 112-92-5

  • 74723-1G

  • 389.61CNY

  • Detail
  • Sigma-Aldrich

  • (74723)  1-Octadecanol  Selectophore, ≥99.5%

  • 112-92-5

  • 74723-5G

  • 1,058.85CNY

  • Detail

112-92-5SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 10, 2017

Revision Date: Aug 10, 2017

1.Identification

1.1 GHS Product identifier

Product name stearyl alcohol

1.2 Other means of identification

Product number -
Other names Octadecan-1-ol

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Food additives -> Flavoring Agents
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:112-92-5 SDS

112-92-5Synthetic route

1-octadecanol
112-92-5

1-octadecanol

(2,6-dichloro-5-methoxyphenyl)-(2,4-dichlorophenyl)methyl octadecyl ether
1205121-90-9

(2,6-dichloro-5-methoxyphenyl)-(2,4-dichlorophenyl)methyl octadecyl ether

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With trifluoroacetic acid In dichloromethane for 4h;100%
stearic acid ethyl ester
111-61-5

stearic acid ethyl ester

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With hydrogen In dodecane at 200℃; under 37503.8 Torr; for 8h; Temperature; Pressure;99.8%
With C30H34Cl2N2P2Ru; potassium methanolate; hydrogen In tetrahydrofuran at 100℃; under 38002.6 - 76005.1 Torr; for 15h; Glovebox; Autoclave;98%
With methanol; sodium tetrahydroborate; sodium ethanolate at 40℃; Reagent/catalyst;72%
Methyl stearate
112-61-8

Methyl stearate

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With sodium tetrahydroborate; N,N-dimethyl-aniline; zinc(II) chloride In tetrahydrofuran for 2h; Heating;99%
With lithium aluminium tetrahydride In toluene at 90℃;98%
With lithium borohydride; 9-methoxy-9-BBN In diethyl ether for 0.5h; Heating;97%
2-(octadecyloxy)tetrahydro-2H-pyran
66938-10-1

2-(octadecyloxy)tetrahydro-2H-pyran

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
poly(4-vinylpyridinium) p-toluenesulfonate In tetrahydrofuran; ethanol at 75℃; for 60h; Hydrolysis;99%
With trichloroisocyanuric acid In methanol at 20℃; for 6h;94%
With iodine In methanol for 0.2h; microwave irradiation;80%
glycerol tristearate
555-43-1

glycerol tristearate

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With C24H38Cl2N3PRu; hydrogen; sodium methylate In isopropyl alcohol at 100℃; under 38002.6 Torr; for 2h; Autoclave;98%
Stage #1: glycerol tristearate With diethylzinc; lithium chloride In tetrahydrofuran; hexane at 20℃; for 6h; Inert atmosphere;
Stage #2: With sodium hydroxide In tetrahydrofuran; hexane; water at 20℃; for 8h; Inert atmosphere; chemoselective reaction;
98%
With 5 wt% Re/TiO2; hydrogen In neat (no solvent) at 230℃; under 37503.8 Torr; for 30h; Autoclave;82%
1-(tert-butyldimethylsilyloxy)octadecan
65598-00-7

1-(tert-butyldimethylsilyloxy)octadecan

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With sodium hydride In N,N,N,N,N,N-hexamethylphosphoric triamide at 25℃; for 10h;97%
With sodium hydrogen sulfate; silica gel In dichloromethane at 20℃; for 0.5h;92%
With ethane-1,2-dithiol; nickel dichloride In methanol; dichloromethane at 20℃; for 0.166667h;90%
trifluoroacetate 1-octadecanol
79392-43-1

trifluoroacetate 1-octadecanol

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With silica gel; triethylamine In diethyl ether; Petroleum ether Substitution; Detrifluoroacetylation;97%
stearic acid
57-11-4

stearic acid

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With 1,1,3,3-Tetramethyldisiloxane; copper(II) bis(trifluoromethanesulfonate) In toluene at 80℃; for 16h; sealed tube;96%
With sodium aluminum tetrahydride In tetrahydrofuran; toluene at 110℃;94%
With sodium tetrahydroborate; benzene-1,2-diol; trifluoroacetic acid In tetrahydrofuran at 25℃; for 4h;94%
stearyl acetate
822-23-1

stearyl acetate

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With methanol; oxo[hexa(trifluoroacetato)]tetrazinc for 12h; Reflux; Inert atmosphere;96%
With 18-crown-6 ether; tert-butylamine In diethyl ether firther solvent;78%
n-Octadecanal
638-66-4

n-Octadecanal

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With water; magnesium; cadmium(II) chloride In tetrahydrofuran for 0.25h;95%
With tri-n-butyl-tin hydride; silica gel In dichloromethane for 24h; Ambient temperature;82%
With acetic acid; zinc und nachfolgende Verseifung des erhaltenen Octadecylacetats mittels alkoholischer Kalilauge;
stearyl trityl ether

stearyl trityl ether

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With sodium hydrogen sulfate; silica gel In methanol; dichloromethane at 20℃; for 3.5h;94%
With lithium chloride In methanol for 12h; Reflux;88%
(1-Methyl-1-octadecyloxy-ethoxymethyl)-benzene
89538-90-9

(1-Methyl-1-octadecyloxy-ethoxymethyl)-benzene

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With hydrogen; palladium on activated charcoal In ethanol under 760 Torr; Ambient temperature;92%
cis-Octadecenoic acid
112-80-1

cis-Octadecenoic acid

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With isopropyl alcohol at 200℃; for 4h; Temperature;91.9%
With cobalt at 135℃; under 147102 Torr; Hydrogenation;
With hydrogen In dodecane at 290℃; under 38002.6 Torr; Activation energy; Autoclave;
oleoyl alcohol
143-28-2

oleoyl alcohol

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With hydrogen; TMSB; palladium In ethanol at 20℃; under 760 Torr; for 42h;91%
With nickel Hydrogenation;
With diethyl ether; hydrogen; platinum
With nickel Hydrogenation;
O-Octadecyl thiobenzoate
57701-11-8

O-Octadecyl thiobenzoate

A

1-octadecanol
112-92-5

1-octadecanol

B

benzyl-octadecyl ether
120726-66-1

benzyl-octadecyl ether

Conditions
ConditionsYield
With 2,2'-azobis(isobutyronitrile); triphenylstannane In toluene at 110℃; for 0.333333h; Yields of byproduct given;A n/a
B 91%
diberomo methyl oleate

diberomo methyl oleate

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With sodium tetrahydroborate In tetrahydrofuran for 2h; Heating;91%
octadecyl adamantane-1-carboxylate

octadecyl adamantane-1-carboxylate

A

1-octadecanol
112-92-5

1-octadecanol

B

octadecane
593-45-3

octadecane

C

1-Adamantanecarboxylic acid
828-51-3

1-Adamantanecarboxylic acid

Conditions
ConditionsYield
With 18-crown-6 ether; tert-butylamine In diethyl etherA 53%
B 40%
C 90%
Octadecanoic acid (1S,7R)-3,5-dioxo-4-aza-tricyclo[5.2.1.02,6]dec-8-en-4-yl ester
77290-17-6

Octadecanoic acid (1S,7R)-3,5-dioxo-4-aza-tricyclo[5.2.1.02,6]dec-8-en-4-yl ester

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With sodium tetrahydroborate In tetrahydrofuran; methanol for 1h; Ambient temperature;90%
4,4,5,5-tetramethyl-2-(octadecyloxy)-1,3,2-dioxaborolane

4,4,5,5-tetramethyl-2-(octadecyloxy)-1,3,2-dioxaborolane

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With water; silica gel In methanol at 60℃; Inert atmosphere;89%
1-(NN-diethylaminothiocarbonyloxy)octadecane
73532-45-3

1-(NN-diethylaminothiocarbonyloxy)octadecane

A

1-octadecanol
112-92-5

1-octadecanol

B

octadecane
593-45-3

octadecane

Conditions
ConditionsYield
With 18-crown-6 ether; tert-butylamine In tetrahydrofuranA 12%
B 87%
With 18-crown-6 ether; tert-butylamine In tetrahydrofuran Ambient temperature;A 12%
B 87%
Octadecanoic acid 2,3,4,5-tetrachloro-6-octadecanoyloxy-phenyl ester
142834-93-3

Octadecanoic acid 2,3,4,5-tetrachloro-6-octadecanoyloxy-phenyl ester

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With sodium tetrahydroborate In tetrahydrofuran 1) 0 deg C, 2 h, 2) rt, 2 h;85%
ethanol
64-17-5

ethanol

stearic acid
57-11-4

stearic acid

A

1-octadecanol
112-92-5

1-octadecanol

B

stearic acid ethyl ester
111-61-5

stearic acid ethyl ester

Conditions
ConditionsYield
With hydrogen at 320℃; under 37503.8 Torr; Pressure; Temperature; Flow reactor;A 83%
B 13%
stearyl trityl ether

stearyl trityl ether

A

1-octadecanol
112-92-5

1-octadecanol

B

trityl chloride
76-83-5

trityl chloride

Conditions
ConditionsYield
With indium; ammonium chloride In methanol for 35h; Reagent/catalyst; Solvent; Temperature; Reflux;A 80%
B 65%
O-Octadecyl thiobenzoate
57701-11-8

O-Octadecyl thiobenzoate

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With 2,2'-azobis(isobutyronitrile); tri-n-butyl-tin hydride In toluene at 110℃; for 0.333333h;77%
2-hexadecyloxirane
7390-81-0

2-hexadecyloxirane

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
With bis(cyclopentadienyl)titanium dichloride; manganese; water In tetrahydrofuran at 20℃; for 24h; Inert atmosphere;75%
octadecyl adamantane-1-carboxylate

octadecyl adamantane-1-carboxylate

A

1-octadecanol
112-92-5

1-octadecanol

B

octadecane
593-45-3

octadecane

Conditions
ConditionsYield
With sodium-potassium alloy; 18-crown-6 ether; tert-butylamine further reagent;A 24%
B 74%
stearic acid
57-11-4

stearic acid

A

1-octadecanol
112-92-5

1-octadecanol

B

hepatdecane
629-78-7

hepatdecane

C

octadecane
593-45-3

octadecane

Conditions
ConditionsYield
With hydrogen In decane at 160℃; under 30003 Torr; for 4h; Temperature; Autoclave;A n/a
B n/a
C 68.39%
With hydrogen In dodecane at 289.84℃; under 6000.6 Torr; for 4h; Autoclave;
With hydrogen In cyclohexane at 179.84℃; under 15001.5 Torr; for 1h; Reagent/catalyst; Pressure; Sealed tube;
n-octadodecyl N-methanesulfonyl thioxocarbamate
175725-46-9

n-octadodecyl N-methanesulfonyl thioxocarbamate

A

1-octadecanol
112-92-5

1-octadecanol

B

O-octadecanylthioxocarbamate

O-octadecanylthioxocarbamate

Conditions
ConditionsYield
With 2,2'-azobis(isobutyronitrile); tri-n-butyl-tin hydride In benzene for 3h; Heating;A 67%
B 23%
1-octadecanol
112-92-5

1-octadecanol

3-tert-butoxycarbonyl-2-chloro-1,3,2-oxazaphospholidine
148160-26-3

3-tert-butoxycarbonyl-2-chloro-1,3,2-oxazaphospholidine

3-tert-butoxycarbonyl-2-octadecyloxy-1,3,2-oxazaphospholidine
148160-29-6

3-tert-butoxycarbonyl-2-octadecyloxy-1,3,2-oxazaphospholidine

Conditions
ConditionsYield
With triethylamine In dichloromethane -40 deg C to r.t., 1 h;100%
1-octadecanol
112-92-5

1-octadecanol

2-chloro-3-methyl-1,3,2-oxazaphospholidine
22082-71-9

2-chloro-3-methyl-1,3,2-oxazaphospholidine

3-Methyl-2-octadecyloxy-1,3,2-oxazaphosphacyclopentane
104702-25-2

3-Methyl-2-octadecyloxy-1,3,2-oxazaphosphacyclopentane

Conditions
ConditionsYield
With triethylamine In dichloromethane for 2h; -40 deg C to RT;100%
With triethylamine In dichloromethane at -60℃; Yield given;
1-octadecanol
112-92-5

1-octadecanol

epichlorohydrin
106-89-8

epichlorohydrin

octadecyl glycidyl ether
16245-97-9

octadecyl glycidyl ether

Conditions
ConditionsYield
With sodium hydroxide; Aliquat 336 In cyclohexane Heating;100%
With sodium hydroxide; Aliquat 336 In cyclohexane Heating;99%
With sodium hydroxide; Aliquat 336 In cyclohexane for 4h; Heating;99%
1-octadecanol
112-92-5

1-octadecanol

acetic anhydride
108-24-7

acetic anhydride

stearyl acetate
822-23-1

stearyl acetate

Conditions
ConditionsYield
With trimethylsilyl trifluoromethanesulfonate In dichloromethane at 0℃; for 0.00833333h;100%
With trimethylsilyl trifluoromethanesulfonate In dichloromethane at 0℃; for 0.00833333h;100%
With silica gel-supported phosphotungstic acid In chloroform at 20℃; for 0.0333333h;98%
1-octadecanol
112-92-5

1-octadecanol

[4-(7-Diethylamino-2-oxo-2H-chromen-3-yl)-phenyl]-oxo-acetonitrile
203256-20-6

[4-(7-Diethylamino-2-oxo-2H-chromen-3-yl)-phenyl]-oxo-acetonitrile

4-(7-Diethylamino-2-oxo-2H-chromen-3-yl)-benzoic acid octadecyl ester

4-(7-Diethylamino-2-oxo-2H-chromen-3-yl)-benzoic acid octadecyl ester

Conditions
ConditionsYield
With dmap In acetonitrile for 1.5h; Heating;100%
1,4-benzenedicarboxylic acid dimethyl ester
120-61-6

1,4-benzenedicarboxylic acid dimethyl ester

1-octadecanol
112-92-5

1-octadecanol

1-methyl-4-octadecyl terephthalate
43049-06-5

1-methyl-4-octadecyl terephthalate

Conditions
ConditionsYield
Stage #1: 1,4-benzenedicarboxylic acid dimethyl ester; 1-octadecanol In xylene for 0.5h; Heating;
Stage #2: With TiO(acac)2 In xylene for 15h; Heating;
100%
1-octadecanol
112-92-5

1-octadecanol

Methyl cinnamate
103-26-4

Methyl cinnamate

octadecyl (2E)-3-phenylprop-2-enoate
61415-12-1

octadecyl (2E)-3-phenylprop-2-enoate

Conditions
ConditionsYield
Stage #1: 1-octadecanol; Methyl cinnamate In xylene for 0.5h; Heating;
Stage #2: With TiO(acac)2 In xylene for 14h; Heating;
100%
1-octadecanol
112-92-5

1-octadecanol

methyl 3-(4-hydroxy-3,5-di-tert-butyl)phenylpropanoate
6386-38-5

methyl 3-(4-hydroxy-3,5-di-tert-butyl)phenylpropanoate

Octadecyl 3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate
2082-79-3

Octadecyl 3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate

Conditions
ConditionsYield
Stage #1: 1-octadecanol; methyl 3-(4-hydroxy-3,5-di-tert-butyl)phenylpropanoate In xylene for 0.5h; Heating;
Stage #2: With TiO(acac)2 In xylene for 11h; Heating;
100%
With sodium montmorillonite In methanol at 110 - 120℃; under 15001.5 - 22502.3 Torr; for 7h; Reagent/catalyst; Inert atmosphere;99.1%
Stage #1: methyl 3-(4-hydroxy-3,5-di-tert-butyl)phenylpropanoate With tetramethoxytitanium; tetrabutoxytitanium In ethylene glycol; toluene for 1.33333h; Inert atmosphere; Cooling with ice;
Stage #2: 1-octadecanol With zirconium (IV) butoxide at 80℃; for 3h; Reagent/catalyst; Temperature; Inert atmosphere; Cooling with ice;
99.6%
1-octadecanol
112-92-5

1-octadecanol

methyl salicylate
119-36-8

methyl salicylate

octadecyl 2-hydroxybenzoate
14971-14-3

octadecyl 2-hydroxybenzoate

Conditions
ConditionsYield
Stage #1: 1-octadecanol; methyl salicylate In xylene for 0.5h; Heating;
Stage #2: With TiO(acac)2 In xylene for 10h; Heating;
100%
1-octadecanol
112-92-5

1-octadecanol

[ethyl undecanoate]-isobutyl-POSS
1021693-09-3

[ethyl undecanoate]-isobutyl-POSS

C57H120O14Si8
1021693-10-6

C57H120O14Si8

Conditions
ConditionsYield
toluene-4-sulfonic acid In toluene for 5h; Heating / reflux;100%
1-octadecanol
112-92-5

1-octadecanol

1-chlorooctadecane
3386-33-2

1-chlorooctadecane

Conditions
ConditionsYield
With hydrogenchloride; N-n-octylalkylpyridinium chlorides; mixture of at 150℃; for 8h; Product distribution / selectivity;99.8%
With Amberlite IRA 93 (PCl5 form) In benzene for 5h; Heating;96%
With hydrogenchloride; trimethyloctadecylammonium chloride for 10h; Irradiation;77%
1-octadecanol
112-92-5

1-octadecanol

ethyl acetate
141-78-6

ethyl acetate

stearyl acetate
822-23-1

stearyl acetate

Conditions
ConditionsYield
With C12F18O13Zn4 for 38h; Reflux; Inert atmosphere;99%
With iodine for 2h; Reflux; chemoselective reaction;98%
With aluminum oxide at 25 - 30℃; for 1h;96%
With copper(II) nitrate for 30h; Heating;85%
With cerium(IV) trifluoromethanesulfonate at 20℃; for 1h; Acetylation;75%
1-octadecanol
112-92-5

1-octadecanol

2,4,4,6-Tetrabromo-2,5-cyclohexadien-1-one
20244-61-5

2,4,4,6-Tetrabromo-2,5-cyclohexadien-1-one

1-Bromooctadecane
112-89-0

1-Bromooctadecane

Conditions
ConditionsYield
With triphenylphosphine In dichloromethane for 4h; Ambient temperature;99%
1-octadecanol
112-92-5

1-octadecanol

acetic acid
64-19-7

acetic acid

stearyl acetate
822-23-1

stearyl acetate

Conditions
ConditionsYield
With sulfonic acid-functionalized periodic mesoporous organosilicas with ethyl bridging group at 60℃; for 24h;99%
With copper(II) nitrate for 3.5h; Heating;90%
With cerium(IV) trifluoromethanesulfonate at 20℃; for 2h; Acetylation;90%
With sulfonic acid immobilized on a periodic mesoporous organosilica with an imidazolium framework In neat (no solvent) at 60℃; for 19h; Green chemistry;90%
1-octadecanol
112-92-5

1-octadecanol

formic acid ethyl ester
109-94-4

formic acid ethyl ester

Octadecyl formate
5451-75-2

Octadecyl formate

Conditions
ConditionsYield
With copper(II) nitrate for 4h; Heating;99%
With cerium(IV) trifluoromethanesulfonate at 20℃; for 0.166667h; Formylation;65%
thiophene-2-carboxylic acid methyl ester
5380-42-7

thiophene-2-carboxylic acid methyl ester

1-octadecanol
112-92-5

1-octadecanol

octadecyl thiophene-2-carboxylate

octadecyl thiophene-2-carboxylate

Conditions
ConditionsYield
Stage #1: thiophene-2-carboxylic acid methyl ester; 1-octadecanol In xylene for 0.5h; Heating;
Stage #2: With TiO(acac)2 In xylene for 13h; Heating;
99%
With iron(III)-acetylacetonate; sodium carbonate In n-heptane at 105℃; for 5h; Inert atmosphere;96%
1-octadecanol
112-92-5

1-octadecanol

4-nitrobenzoic acid methyl ester
619-50-1

4-nitrobenzoic acid methyl ester

octadecyl 4-nitro-benzoate
56426-96-1

octadecyl 4-nitro-benzoate

Conditions
ConditionsYield
Stage #1: 1-octadecanol; 4-nitrobenzoic acid methyl ester In xylene for 0.5h; Heating;
Stage #2: With TiO(acac)2 In xylene for 4.5h; Heating;
99%
1-octadecanol
112-92-5

1-octadecanol

4-methoxycarbonylphenyl bromide
619-42-1

4-methoxycarbonylphenyl bromide

4-Brombenzoesaeure-n-octadecylester
70153-15-0

4-Brombenzoesaeure-n-octadecylester

Conditions
ConditionsYield
Stage #1: 1-octadecanol; 4-methoxycarbonylphenyl bromide In xylene for 0.5h; Heating;
Stage #2: With TiO(acac)2 In xylene for 5h; Heating;
99%
cycl-isopropylidene malonate
2033-24-1

cycl-isopropylidene malonate

1-octadecanol
112-92-5

1-octadecanol

Conditions
ConditionsYield
at 115℃; for 3h;99%
Stage #1: cycl-isopropylidene malonate; 1-octadecanol In toluene for 4h; Reflux;
Stage #2: With sodium hydrogencarbonate In water; toluene at 20℃;
Stage #3: With hydrogenchloride In water
96%
at 110 - 120℃; for 1h;93%
1-octadecanol
112-92-5

1-octadecanol

bis(trichloromethyl) carbonate
32315-10-9

bis(trichloromethyl) carbonate

stearyl chloroformate
51637-93-5

stearyl chloroformate

Conditions
ConditionsYield
With pyridine In tetrachloromethane at -15 - 40℃; Product distribution / selectivity;99%
With pyridine In dichloromethane at 10 - 15℃; for 2h; Cooling with ice;83%
Stage #1: bis(trichloromethyl) carbonate With potassium carbonate; N,N-dimethyl-formamide In toluene at 0℃; for 0.5h; Inert atmosphere;
Stage #2: 1-octadecanol In toluene at 0 - 20℃; for 12h; Inert atmosphere;
75%
With pyridine In tetrachloromethane at -20 - 20℃;
1-octadecanol
112-92-5

1-octadecanol

3-phenylpropanoic acid methyl ester
103-25-3

3-phenylpropanoic acid methyl ester

octadecyl 3-phenylpropionate
120703-15-3

octadecyl 3-phenylpropionate

Conditions
ConditionsYield
With Zn4(OCOCF3)6O In di-isopropyl ether for 18h; Heating;99%
With potassium phosphate; N-benzyl-N,N,N-triethylammonium chloride In toluene for 48h; Reflux;69%
1-octadecanol
112-92-5

1-octadecanol

(E)-3-phenylacrylic acid
140-10-3

(E)-3-phenylacrylic acid

octadecyl (2E)-3-phenylprop-2-enoate
61415-12-1

octadecyl (2E)-3-phenylprop-2-enoate

Conditions
ConditionsYield
With triphenylphosphine; diethylazodicarboxylate In tetrahydrofuran at 20℃; Mitsunobu reaction;99%
1-octadecanol
112-92-5

1-octadecanol

(+-)-2-methyl-pent-4-enoic acid
1575-74-2

(+-)-2-methyl-pent-4-enoic acid

octadecyl 2-methylpent-4-enoate

octadecyl 2-methylpent-4-enoate

Conditions
ConditionsYield
With dmap; dicyclohexyl-carbodiimide In dichloromethane at 0 - 20℃; Steglich Esterification;99%
1-octadecanol
112-92-5

1-octadecanol

octadecanoic acid, octadecyl ester
2778-96-3

octadecanoic acid, octadecyl ester

Conditions
ConditionsYield
With sodium bromate; sulfuric acid; sodium bromide In water at 20℃; for 24h;99%
With (bis[(2-diisopropylphosphino)ethyl]amine)Mn(CO)2 at 150℃; for 24h; Catalytic behavior; Inert atmosphere;80 %Spectr.
1-octadecanol
112-92-5

1-octadecanol

1,12-dodecanedioic acid
693-23-2

1,12-dodecanedioic acid

distearyl dodecanedioate
42234-06-0

distearyl dodecanedioate

Conditions
ConditionsYield
With 1-hexadecyl-3-sulfo-1H-imidazol-3-ium chloride In neat (no solvent) at 110℃; for 16h; Green chemistry;99%

112-92-5Relevant articles and documents

Selective Hydrodeoxygenation of Vegetable Oils and Waste Cooking Oils to Green Diesel Using a Silica-Supported Ir–ReOx Bimetallic Catalyst

Liu, Sibao,Simonetti, Trent,Zheng, Weiqing,Saha, Basudeb

, p. 1446 - 1454 (2018)

High yields of diesel-range alkanes are prepared by hydrodeoxygenation of vegetable oils and waste cooking oils over ReOx-modified Ir/SiO2 catalysts under mild reaction conditions. The catalyst containing a Re/Ir molar ratio of 3 exhibits the best performance, achieving 79–85 wt % yield of diesel-range alkanes at 453 K and 2 MPa H2. The yield is nearly quantitative for the theoretical possible long-chain alkanes on the basis of weight of the converted oils. The catalyst retains comparable activity upon regeneration through calcination. Control experiments using probe molecules as model substrates suggest that C=C bonds of unsaturated triglycerides and free fatty acids are first hydrogenated to their corresponding saturated intermediates, which are then converted to aldehyde intermediates through hydrogenolysis of acyl C?O bonds and subsequently hydrogenated to fatty alcohols. Finally, long-chain alkanes without any carbon loss are formed by direct hydrogenolysis of the fatty alcohols. Small amounts of alkanes with one carbon fewer are also formed by decarbonylation of the aldehyde intermediates. A synergy between Ir and partially reduced ReOx sites is discussed to elucidate the high activity of Ir–ReOx/SiO2.

An unconventional DCOx favored Co/N-C catalyst for efficient conversion of fatty acids and esters to liquid alkanes

Li, Jiang,Liu, Jiaxing,Zhang, Junjie,Wan, Tong,Huang, Lei,Wang, Xintian,Pan, Runze,An, Zhidong,Vlachos, Dionisios G.

, (2020)

Cobalt (Co) catalysis has recently attracted significant attention in the field of biomass conversion. However, the fabrication of highly dispersive Co nanoparticles at high metal loading with selective facet exposure to achieve specific selectivity is still questionable. In this work, a nitrogen-doped carbon-supported Co catalyst is fabricated for efficient conversion of fatty acids and esters to liquid alkanes. Nitrogen-doping facilitates a highly uniform dispersion of Co nanoparticles even at a high Co loading of 10 wt% and after recycling for 5 runs. The Co/N-C catalyst affords an unconventional decarbonylation/decarboxylation (DCOx) dominant selectivity probably due to partial reduction of cobalt oxides to α-Co0 with only exposure of the (111) facet. Co-existence of Co and N-C leads to strong Lewis acidity and basicity, facilitating the interaction between catalyst and –COOH group, and some important acid-catalyzed step-reactions. The versatility of the Co/N-C catalyst is demonstrated through conversion of various fatty acids and esters.

Permeable composite membrane as a catalytically active contactor for hydrogenation reactions

Minyukova, T. P.,Shtertser, N. V.,Khassin, A. A.,Yurieva, T. M.

, p. 107 - 110,4 (2012)

The efficiency of using of the permeable composite membrane (PCM) is demonstrated in the 3-phase reaction of liquid substrate with gaseous hydrogen on solid catalyst (PCM acts as a catalytically active contactor) - hydrogenation of fatty acid triglyceride. PCM provides a good combination of the opposite requirements of mild internal diffusion restrictions, low hydraulic resistance, high thermal conductivity, well-developed gas-liquid interface and high catalyst loading in the reactor volume, and thus assures the control of the course of the catalytic reaction.

Highly Selective Hydrodecarbonylation of Oleic Acid into n-Heptadecane over a Supported Nickel/Zinc Oxide-Alumina Catalyst

Li, Guangci,Zhang, Feng,Chen, Lei,Zhang, Chuanhui,Huang, He,Li, Xuebing

, p. 2646 - 2653 (2015)

The production of second-generation biodiesel with triglycerides or their derivatives through hydroprocessing is considered as a promising approach to make transportation fuels. In this study, a series of Ni-based catalysts supported on basic composite oxides (MO-Al2O3, M=Mg, Ca, Ni, Cu, Zn) were prepared for the catalytic deoxygenation of oleic acid in the presence of H2. Ni/ZnO-Al2O3 exhibited the highest deoxygenation activity and alkane selectivity, which depended on its moderate basicity. Investigations of the reaction conditions, which include reaction time, reaction temperature, H2 pressure, and Ni loading, suggested that n-heptadecane was the predominant product and its content increased with reaction temperature. The reaction temperature was more important than H2 pressure in the catalytic deoxygenation of oleic acid. Additionally, the overall reaction pathways for the conversion of oleic acid were proposed based on the product distribution for different durations and reaction rates of stearic acid, 1-octadecanol, and stearyl stearate, in which the oxygen atoms in the oleic acid were mainly removed in the form of CO through a hydrogenation-dehydrogenation-decarbonylation reaction route. If glycerol trioleate was used instead of oleic acid, Ni/ZnO-Al2O3 exhibited a high hydrodecarbonylation activity and selectivity to n-heptadecane.

Influence of the operating conditions and kinetic analysis of the selective hydrogenation of oleic acid on Ru-Sn-B/Al2O3 catalysts

Sánchez, María A.,Pouilloux, Yannick,Mazzieri, Vanina A.,Pieck, Carlos L.

, p. 552 - 558 (2013)

The influence of the operating conditions on the selectivity and activity of Ru-Sn-B/Al2O3 catalysts for the hydrogenation of oleic acid to oleyl alcohol was studied. It was found that the Ru-Sn-B/Al 2O3 catalyst is selective to oleyl alcohol while Ru or Ru-B/Al2O3 catalysts are not selective to produce oleyl alcohol. The electronic and catalytic properties of Ru are modified by the strong interaction between Sn and B. The incorporation of Sn leads to catalysts capable of producing oleyl alcohol. The experiments of oleic acid hydrogenation showed that an increase in reaction temperature leads to an increase in activity while the selectivity to oleyl alcohol goes through a maximum. This is because the reactions of hydrogenation of CC double bond have lower activation energies than hydrogenolytic reactions. The increase in operating pressure has a positive effect on conversion and a more important effect on selectivity. A very simple first order kinetic model is proposed and reasonably represents the results obtained. This model can be useful to compare catalyst performance more rationally.

Synergistic Interaction between Oxides of Copper and Iron for Production of Fatty Alcohols from Fatty Acids

Kandel, Kapil,Chaudhary, Umesh,Nelson, Nicholas C.,Slowing, Igor I.

, p. 6719 - 6723 (2015)

The selective hydrogenation of fatty acids to fatty alcohols can be achieved under moderate conditions (180 °C, 30 bar H2) by simultaneously supporting copper and iron oxides on mesoporous silica nanoparticles. The activity of the cosupported oxides is significantly higher than that of each supported metal oxide and of a physical mixture of both individually supported metal oxides. A strong interaction between both metal oxides is evident from dispersion, XRD, TPR, and acetic acid TPD measurements, which is likely responsible for the synergistic behavior of the catalyst. Copper oxide is reduced in situ to its metallic form and thereby activates hydrogen. It is proposed that hydrogen spills over to iron oxide where fatty acids bind and are selectively reduced to the alcohol.

Kinetics of hydrodeoxygenation of stearic acid using supported nickel catalysts: Effects of supports

Kumar, Pankaj,Yenumala, Sudhakara Reddy,Maity, Sunil K.,Shee, Debaprasad

, p. 28 - 38 (2014)

The hydrodeoxygenation of fatty acids derived from vegetable and microalgal oils is a novel process for production of liquid hydrocarbon fuels well-suited with existing internal combustion engines. The hydrodeoxygenation of stearic acid was investigated in a high pressure batch reactor using n-dodecane as solvent over nickel metal catalysts supported on SiO2, γ-Al2O3, and HZSM-5 in the temperature range of 533-563 K. Several supported nickel oxide catalysts with nickel loading up to 25 wt.% were prepared by incipient wetness impregnation method and reduced using hydrogen. The catalysts were then characterized by BET, TPR, H2 pulse chemisorption, TPD, XRD, and ICP-AES. Characterization studies revealed that only dispersed nickel oxide was present up to 15 wt.% nickel loading on γ-Al2O3. The acidity of the supports depends on nickel loading of oxidized catalysts and increases with increasing nickel loading up to 15 wt.%. n-Pentadecane, n-hexadecane, n-heptadecane, n-octadecane, and l-octadecanol were identified as products of hydrodeoxygenation of stearic acid with n-heptadecane being primary product. The catalytic activity and selectivity to products for hydrodeoxygenation of stearic acid depends strongly on acidity of the supports. The maximum selectivity to n-heptadecane was observed with nickel supported γ-Al2O3 catalyst. A suitable reaction mechanism of hydrodeoxygenation of stearic acid was delineated based on products distribution. The conversion of stearic acid was increased with increasing reaction time, nickel loading on γ-Al2O 3, temperature, and catalyst loading. Complete conversion of stearic acid was accomplished with more than 80% selectivity to n-heptadecane at reasonable reaction temperature of 563 K after 240 min of reaction using 15 wt.% Ni/γ-Al2O3 catalyst. An empirical kinetic model was also developed to correlate the experimental data.

The selective hydrogenation of ethyl stearate to stearyl alcohol over Cu/Fe bimetallic catalysts

He, Limin,Li, Xiaoru,Lin, Weiwei,Li, Wei,Cheng, Haiyang,Yu, Yancun,Fujita, Shin-Ichiro,Arai, Masahiko,Zhao, Fengyu

, p. 143 - 149 (2014)

Bimetallic and monometallic catalysts including Cu and/or Fe species were prepared by a co-precipitation method and their catalytic performance was tested for the selective hydrogenation of ethyl stearate to stearyl alcohol. The bimetallic catalysts were observed to be even more active for this selective hydrogenation compared to the monometallic catalysts and their physical mixtures. With a bimetallic catalyst of Cu/Fe (4/1 in mole ratio) reduced at 200 °C, a selectivity to the alcohol reached to above 99% at a conversion of 97% in reaction for 4 h at 230°C, 3.0 MPa. Effects of composition and reduction temperature on the catalytic performance were studied and the properties of catalysts prepared under different conditions were examined by XRD, TPR, N2 physisorption, and SEM. The relationship of the performance with the properties of the catalysts was discussed, along with the conditions under which synergistic effects of Cu and Fe species appeared and caused the enhancement of the catalytic performance.

An efficient hydrogenation catalytic model hosted in a stable hyper-crosslinked porous-organic-polymer: From fatty acid to bio-based alkane diesel synthesis

Sarkar, Chitra,Shit, Subhash Chandra,Dao, Duy Quang,Lee, Jihyeon,Tran, Ngoc Han,Singuru, Ramana,An, Kwangjin,Nguyen, Dang Nam,Le, Quyet Van,Amaniampong, Prince Nana,Drif, Asmaa,Jerome, Francois,Huyen, Pham Thanh,Phan, Thi To Nga,Vo, Dai-Viet N.,Thanh Binh, Nguyen,Trinh, Quang Thang,Sherburne, Matthew P.,Mondal, John

, p. 2049 - 2068 (2020)

In this study, a Pd-based catalytic model over a nitrogen enriched fibrous Porous-Organic-Polymer (POP) is established to execute hydrodeoxygenation of various vegetable oils in producing potential large-scale renewable diesel. Here we report a cost-effective synthesis strategy for a new microporous hypercrosslinked POP through the FeCl3 assisted Friedel-Crafts alkylation reaction, followed by fabrication of Pd0-NPs (2-3 nm) using a solid gas phase hydrogenation route to deliver a novel catalytic system. This catalyst (called Pd@PPN) exhibits versatile catalytic performance for different types of vegetable oils including palm oil, soybean oil, sunflower oil and rapeseed oil to furnish long chain diesel range alkanes. The catalyst is comprehensively characterized using various spectroscopic tools and it shows high stability during five runs of recycling without leaching of Pd. Our results further reveal that a direct decarbonylation (DCN) pathway of fatty acids to produce alkanes with one fewer carbon is the dominant mechanism. Under optimized conditions, using stearic acid to represent the long linear carboxylic acids in the vegetable oils, up to 90% conversion with 83% selectivity of C17-alkane has been achieved on our fabricated catalyst. Density functional theory (DFT) calculations are performed to provide insights into the electronic properties of the catalyst, the mechanistic reaction pathway, the crucial role of the catalyst surface and the product selectivity trend. The strong interaction between the corrugated polymer-frame-structure and the Pd-NPs suggests the presence of high density step sites on the fabricated Pd-NP anchored within the cage of the polymer structure. DFT calculations also reveal the strong promotional effect of step sites and charge transfer in facilitating rate-limiting steps during the decarbonylation (DCN) pathway and removal of strongly bound intermediates formed during the process, therefore explaining the high activity of the fabricated Pd@PPN catayst for the hydrodeoxygenation (HDO) conversion to produce bio-based alkane diesel.

Spectroscopy and Reactivity of Dialkoxy Acenes

Brega, Valentina,Kanari, Sare Nur,Doherty, Connor T.,Che, Dante,Sharber, Seth A.,Thomas, Samuel W.

, p. 10400 - 10407 (2019)

Photochemical oxidation of acenes can benefit or impede their function, depending on the application. Although acenes with alkoxy substituents on reactive sites are important for applications as diverse as drug delivery and organic optoelectronics, the influence of chemical structure on their photochemical oxidation remains unknown. This paper therefore describes the synthesis, spectroscopic properties, and reactivity with singlet oxygen (1O2) of a series of dialkoxyacenes that vary in the number and types of fused rings in the (hetero)acene cores. Reductive alkylation of quinone precursors yielded target dialkoxyacenes with fused backbones ranging from benzodithiophene to tetracenothiophene. Trends of their experimental spectroscopic characteristics were consistent with time-dependent density functional theory (TD-DFT) calculations. NMR studies show that photochemically generated 1O2 oxidizes all but one of these acenes to the corresponding endoperoxides in organic solvent. The rates of these oxidations correlate with the number and types of fused arenes, with longer dialkoxyacenes generally oxidizing faster than shorter derivatives. Finally, irradiation of these acenes in acidic, oxidizing environments cleaves the ether bonds. This work impacts those working in organic optoelectronics, as well as those interested in harnessing photogenerated reactive oxygen species in functional materials.

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