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Raney nickel , also called spongy nickel, is a fine-grained solid composed mostly of derived from a nickel– alloy.

(2025). 9780471396987, Wiley-Interscience. .
Several grades are known, of which most are gray solids. Some are , but most are used as air-stable slurries. Raney nickel is used as a reagent and as a catalyst in organic chemistry. It was developed in 1926 by American engineer for the of vegetable oils.'''See:
  • Raney, Murray, "Method of producing finely-divided nickel," U.S. patent 1,628,190 (filed: 14 May 1926 ; issued: 10 May 1927).
  • M. S. Wainwright, "3.2 Skeletal metal catalysts" in: Gerhard Ertl, Helmut Knözinger, and Jens Weitkamp, ed.s, Preparation of Solid Catalysts (Weinheim, Federal Republic of Germany: Wiley-VCH Verlag, 1999), pages 28–29.'''
Raney Nickel is a registered trademark of W. R. Grace and Company. Other major producers are and .


Preparation

Alloy preparation
The Ni–Al alloy is prepared by dissolving nickel in molten aluminium followed by cooling ("quenching"). Depending on the Ni:Al ratio, quenching produces a number of different phases. During the quenching procedure, small amounts of a third metal, such as zinc or chromium, are added to enhance the activity of the resulting catalyst. This third metal is called a "promoter".
(1997). 9783527298266, Wiley. .
The promoter changes the mixture from a binary alloy to a ternary alloy, which can lead to different quenching and leaching properties during activation.


Activation
In the activation process, the alloy, usually as a fine powder, is treated with a concentrated solution of . The simplified leaching reaction is given by the following chemical equation:

2 Al + 2 NaOH + 6 H2O → 2 NaAl(OH)4 + 3 H2
The formation of (NaAl(OH)4) requires that solutions of high concentration of sodium hydroxide be used to avoid the formation of aluminium hydroxide, which otherwise would precipitate as . Hence sodium hydroxide solutions with concentrations of up to 5 M are used.

The temperature used to leach the alloy has a marked effect on the properties of the catalyst. Commonly, leaching is conducted between 70 and 100 °C. The surface area of Raney nickel (and related catalysts in general) tends to decrease with increasing leaching temperature. This is due to structural rearrangements within the alloy that may be considered analogous to , where alloy ligaments would start adhering to each other at higher temperatures, leading to the loss of the porous structure.

During the activation process, Al is leached out of the NiAl3 and Ni2Al3 phases that are present in the alloy, while most of the Ni remains, in the form of NiAl. The removal of Al from some phases but not others is known as "selective leaching". The NiAl phase has been shown to provide the structural and thermal stability of the catalyst. As a result, the catalyst is quite resistant to decomposition ("breaking down", commonly known as "aging"). This resistance allows Raney nickel to be stored and reused for an extended period; however, fresh preparations are usually preferred for laboratory use.

(1993). 9780444890634, Elsevier. .
For this reason, commercial Raney nickel is available in both "active" and "inactive" forms.

Before storage, the catalyst can be washed with distilled water at ambient temperature to remove remaining sodium aluminate. Oxygen-free () water is preferred for storage to prevent of the catalyst, which would accelerate its aging process and result in reduced catalytic activity.


Properties
Macroscopically, Raney nickel is a finely divided, grey powder. Microscopically, each particle of this powder is a three-dimensional , with pores of irregular size and shape, the vast majority of which are created during the leaching process. Raney nickel is notable for being thermally and structurally stable, as well as having a large -Emmett- () surface area. These properties are a direct result of the activation process and contribute to a relatively high catalytic activity.

The surface area is typically determined by a BET measurement using a gas that is preferentially adsorbed on metallic surfaces, such as . Using this type of measurement, almost all the exposed area in a particle of the catalyst has been shown to have Ni on its surface. Since Ni is the active metal of the catalyst, a large Ni surface area implies a large surface area is available for reactions to occur simultaneously, which is reflected in an increased catalyst activity. Commercially available Raney nickel has an average Ni surface area of 100 m2 per gram of catalyst.

A high catalytic activity, coupled with the fact that hydrogen is absorbed within the pores of the catalyst during activation, makes Raney nickel a useful catalyst for many reactions. Its structural and thermal stability (i.e., it does not decompose at high temperatures) allows its use under a wide range of reaction conditions.

(1986). 9780521311175, Cambridge University Press. .
Additionally, the of Raney nickel is negligible in most common laboratory solvents, with the exception of such as hydrochloric acid, and its relatively high density (about 6.5 g cm−3) also facilitates its separation from a liquid phase after a reaction is completed.


Applications
Raney nickel is used in a large number of industrial processes and in organic synthesis because of its stability and high catalytic activity at room temperature.


Industrial applications
In a commercial application, Raney nickel is used as a catalyst for the of to . Other heterogeneous catalysts, such as those using are used in some cases. Platinum metals tend to be more active, requiring milder temperatures, but they are more expensive than Raney nickel. The cyclohexane thus produced may be used in the synthesis of , a raw material used in the industrial production of such as nylon.
(2025). 9780471417996, Wiley. .

Other industrial applications of Raney nickel include the conversion of:


Applications in organic synthesis

Desulfurization
Raney nickel is used in organic synthesis for . For example, will be reduced to hydrocarbons in the last step of the Mozingo reduction:
(2025). 9780199270293, Oxford University Press.

, and can be removed from , , or heteroaromatic compounds. Likewise, Raney nickel will remove the sulfur of to give a saturated .


Reduction of functional groups
It is typically used in the of compounds with multiple bonds, such as , , , , and -containing compounds. Additionally, Raney nickel will reduce heteroatom-heteroatom bonds, such as , groups, and nitrosamines. It has also found use in the reductive of and the of alcohols.

When reducing a carbon-carbon double bond, Raney nickel will add hydrogen in a fashion.


Related catalysts
Raney cobalt has also been described.

In contrast to the pyrophoric nature of some forms of Raney nickel, -based catalysts represent potentially safer alternatives.

Raney alloys include FeTi and other non Nickel alloys. FeTi has been considered for low pressure Hydrogen Storage. Aldricimica Acta (free from Sigma nee Aldrich) has a complete list of Raney alloys.


Safety
Due to its large surface area and high volume of contained hydrogen gas, dry, activated Raney nickel is a material that requires handling under an inert atmosphere. Raney nickel is typically supplied as a 50% in water. Even after reaction, residual Raney nickel contains significant amounts of hydrogen gas and may spontaneously ignite when exposed to air.
(2025). 9781566705677, CRC Press. .

Additionally, acute exposure to Raney nickel may cause irritation of the respiratory tract and nasal cavities, and causes pulmonary fibrosis if inhaled. Ingestion may lead to convulsions and intestinal disorders. It can also cause eye and skin irritation. Chronic exposure may lead to and other signs of to nickel, such as skin rashes ("nickel itch").

Nickel is also rated as being a possible human by the IARC (Group 2B, EU category 3) and , while the inhalation of fine particles is associated with Shaver's disease.


Development
graduated as a mechanical engineer from the University of Kentucky in 1909. In 1915 he joined the Lookout Oil and Refining Company in Tennessee and was responsible for the installation of electrolytic cells for the production of hydrogen which was used in the of vegetable oils. During that time the industry used a nickel catalyst prepared from nickel(II) oxide. Believing that better catalysts could be produced, around 1921 he started to perform independent research while still working for Lookout Oil. In 1924 a 1:1 ratio Ni/ alloy was produced, which after treatment with sodium hydroxide, was found to be five times more active than the best catalyst used in the hydrogenation of cottonseed oil. A patent for this discovery was issued in December 1925. (Raney's original nickel-silicon catalyst)

Subsequently, Raney produced a 1:1 Ni/Al alloy following a procedure similar to the one used for the nickel-silicon catalyst. He found that the resulting catalyst was even more active and filed a patent application in 1926. This is now a common alloy composition for modern Raney nickel catalysts. Other common alloy compositions include 21:29 Ni/Al and 3:7 Ni/Al. Both the activity and preparation protocols for these catalysts vary.

Following the development of Raney nickel, other alloy systems with aluminium were considered, of which the most notable include copper, and .

(1996). 9780824790219, CRC Press. .
Further research showed that adding a small amount of a third metal to the binary alloy would promote the activity of the catalyst. Some widely used promoters are zinc, and . An alternative way of preparing Raney nickel has been devised by surface of .


See also
  • Urushibara nickel
  • Nickel boride catalyst
  • , a similar cobalt/aluminum alloy catalyst which is sometimes more selective for certain hydrogenation products (e.g. primary via nitrile reduction).


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