# US 5,705,684 A · Preparation of acrolein, acrylic acid or a mixture thereof from propane

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- Number: US 5,705,684 A
- Document ID: US5705684A
- Status: Granted
- Kind: A
- Application number: 08/618,440
- Filed: 1996-03-08
- Granted: 1998-01-06
- Earliest claimed: 1995-03-10
- Assignees: BASF SE
- Inventors: Werner Hefner; Otto Machhammer; Hans-Peter Neumann; Andreas Tenten; Wilhelm Ruppel; Herbert Vogel
- Web page: https://patentgrep.com/patent/US5705684A

## CPC

- C07C 45/35: in propene or isobutene
- C07C 45/33: of CHx-moieties
- C07C 51/252: {of propene, butenes, acrolein or methacrolein}
- C07C: ACYCLIC OR CARBOCYCLIC COMPOUNDS

## Abstract

In a process for preparing acrolein, acrylic acid or a mixture thereof from propane, propane is partially dehydrogenated to propylene in a first stage, the product gas mixture resulting therefrom is, after separating off hydrogen and water vapor, used as feed to an oxidation reactor, the propylene formed in the dehydrogenation is partially oxidized in the oxidation reactor using molecular oxygen in the presence of non-dehydrogenated propane as inert diluent gas to give acrolein, acrylic acid or a mixture thereof and the propane present in the product gas mixture of the partial oxidation is subsequently recirculated to the dehydrogenation stage A.

## Claims

### Claim 1

A process for preparing acrolein, acrylic acid or a mixture thereof from propane, in which
A) in a first stage A, the propane is subjected to a partial heterogeneously catalyzed dehydrogenation in the gas phase to give propylene,
B) the product gas mixture from stage A containing propylene and unreacted propane is used in a second stage B as feed to an oxidation reactor and in the oxidation reactor the propylene is subjected to a selective heterogeneously catalyzed gas-phase partial oxidation with molecular oxygen to give acrolein, acrylic acid or a mixture thereof as target product, with pure oxygen being used as oxygen source, and
C) in a third stage C, the target product is separated from the product gas stream obtained from the partial oxidation of the propylene in stage B and at least the unreacted propane present in the product gas stream from stage B is recirculated to the dehydrogenation stage A,
wherein, from among the constituents other than propane and propylene present in the product gas mixture from stage A, at least the hydrogen and the water vapor are separated from the product gas mixture before it is used as feed to the oxidation reactor of the second stage B.

### Claim 2 (depends on 1)

A process as claimed in claim 1, wherein the total amount of constituents other than propane and propylene present in the product gas mixture of stage A are removed therefrom before it is used as feed to the oxidation reactor of the second stage B.

### Claim 3 (depends on 1)

A process as claimed in claim 1, wherein the stage B is implemented in the form of two oxidation reactors connected in series, of which the first is charged with a multimetal oxide catalyst containing the element combination Mo--Bi--Fe and the second is charged with a multimetal oxide catalyst containing the element combination Mo--V.

### Claim 4 (depends on 3)

A process as claimed in claim 3, wherein the product gas mixture of the first oxidation reactor is transferred without intermediate treatment to the second oxidation reactor, with the volume ratio of organic compound to be partially oxidized (propylene or acrolein) :molecular oxygen being set at 1:1 to 3 in the feed gas mixtures of both oxidation reactors.