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1004-29-1

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1004-29-1 Usage

General Description

2-Butyltetrahydrofuran is a chemical compound that is classified as an organic, heterocyclic compound. It has a five-membered ring comprising four carbon atoms and one oxygen atom. Additionally, it has a butyl group attached at the second carbon in the cyclic chain. 2-butyltetrahydrofuran is a type of ether and is commonly used as a solvent in the production of chemicals. 2-Butyltetrahydrofuran is also used in certain pharmaceuticals. Despite its broad usage, it is important to handle and store this chemical appropriately due to its potential to cause eye and skin irritation, and its harmfulness if swallowed or inhaled. Its CAS number is 118-39-8.

Check Digit Verification of cas no

The CAS Registry Mumber 1004-29-1 includes 7 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 4 digits, 1,0,0 and 4 respectively; the second part has 2 digits, 2 and 9 respectively.
Calculate Digit Verification of CAS Registry Number 1004-29:
(6*1)+(5*0)+(4*0)+(3*4)+(2*2)+(1*9)=31
31 % 10 = 1
So 1004-29-1 is a valid CAS Registry Number.
InChI:InChI=1/C8H16O/c1-2-3-5-8-6-4-7-9-8/h8H,2-7H2,1H3

1004-29-1SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 13, 2017

Revision Date: Aug 13, 2017

1.Identification

1.1 GHS Product identifier

Product name 2-butyltetrahydrofuran

1.2 Other means of identification

Product number -
Other names Furan, 2-butyltetrahydro-

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:1004-29-1 SDS

1004-29-1Relevant articles and documents

Tailor-made biofuel 2-butyltetrahydrofuran from the continuous flow hydrogenation and deoxygenation of furfuralacetone

Strohmann, Marc,Bordet, Alexis,Vorholt, Andreas J.,Leitner, Walter

, p. 6299 - 6306 (2019)

In this work, we present the first continuous flow process to produce the tailored biofuel 2-butyltetrahydrofuran from renewable resources. In a two-step approach lignocellulose-derived furfuralacetone is first hydrogenated and then deoxygenated over commercial catalysts to form the desired product. Both reactions were studied independently in batch conditions. The transition to a continuous flow system was done and various parameters were tested in the miniplant. Both reactions were performed in a two-reactor-concept approach to yield the desired 2-butyltetrahydrofuran in a high yield directly from furfuralacetone.

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Micovic et al.

, p. 2279,2286 (1964)

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SELECTIVITY OF TETRAHYDROFURAN FORMATION FROM UNACTIVATED ALIPHATIC ALCOHOLS BY THE BROMINE-SILVER-SALT REACTION

Roscher, Nina Matheny,Shaffer, D. Kent

, p. 2643 - 2650 (1984)

Studies of the bromine-silver carbonate reaction with aliphatic alcohols in which intramolecular δ-H competition is possible are generally quite specific.Loss of a tertiary δ- hydrogen occurs preferentially from both tertiary and secondary aliphatic alcohols to yield the most highly substituted cyclic ether.For example, 2,5-dimethyl-2-octanol yields only 2,2,5-trimethyl-5-propyltetrahydrofuran as the cyclic ether product; 2-methyl-2-isopentyltetrahydrofuran is not detected.

Energy-efficient production of 1-octanol from biomass-derived furfural-acetone in water

Xia, Qineng,Xia, Yinjiang,Xi, Jinxu,Liu, Xiaohui,Wang, Yanqin

, p. 4411 - 4417 (2015)

An energy-efficient catalytic system for the one-pot production of 1-octanol from biomass-derived furfural-acetone (FFA) under mild conditions in water was developed, by sequential hydrogenation/hydrogenolysis over a hydrophilic Pd/NbOPO4 catalyst. A strategy of creating an intentional "phase problem" has been employed to prevent the over-hydrogenolysis of 1-octanol into n-octane and therefore increased the selectivity to 1-octanol. The effects of reaction conditions as well as a variety of noble-metal loaded bifunctional catalysts have been systematically investigated to maximize the yield of 1-octanol. Moreover, the addition of liquid acids to the catalytic system further enhanced the selectivity towards the formation of 1-octanol. There is a strong correlation between the acid strength of an acidic additive and the sum yield of 1-octanol and octane. With the addition of TfOH, the highest yield of 1-octanol (62.7%) was obtained from one-pot conversion of biomass-derived FFA over Pd/NbOPO4.

Selective Hydrogenation and Hydrodeoxygenation of Aromatic Ketones to Cyclohexane Derivatives Using a Rh&at;SILP Catalyst

Bordet, Alexis,Emondts, Meike,Leitner, Walter,Moos, Gilles

supporting information, p. 11977 - 11983 (2020/06/02)

Rhodium nanoparticles immobilized on an acid-free triphenylphosphonium-based supported ionic liquid phase (Rh&at;SILP(Ph3-P-NTf2)) enabled the selective hydrogenation and hydrodeoxygenation of aromatic ketones. The flexible molecular approach used to assemble the individual catalyst components (SiO2, ionic liquid, nanoparticles) led to outstanding catalytic properties. In particular, intimate contact between the nanoparticles and the phosphonium ionic liquid is required for the deoxygenation reactivity. The Rh&at;SILP(Ph3-P-NTf2) catalyst was active for the hydrodeoxygenation of benzylic ketones under mild conditions, and the product distribution for non-benzylic ketones was controlled with high selectivity between the hydrogenated (alcohol) and hydrodeoxygenated (alkane) products by adjusting the reaction temperature. The versatile Rh&at;SILP(Ph3-P-NTf2) catalyst opens the way to the production of a wide range of high-value cyclohexane derivatives by the hydrogenation and/or hydrodeoxygenation of Friedel–Crafts acylation products and lignin-derived aromatic ketones.

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