IP Library Granted Patent US 7,368,482
Granted Patent B2
US 7,368,482 · App. 10/571,538 · Granted May 6, 2008

Catalytic partial oxidation process for producing synthesis gas

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Quick Facts
Patent No.
US 7,368,482
App. No.
10/571,538
Granted
May 6, 2008
Kind
B2
Abstract

Partial oxidation process of liquid fuels, selected from hydrocarbon and/or oxygenated compounds, together with gaseous fuels, selected from hydrocarbon compounds, natural gas and LPG, by means of a suitable catalytic system comprising the following steps: premixing the reagents and possibly heating them to temperatures ranging from 25 to 400° C., said reagents consisting of said liquid fuels, said gaseous fuels and oxygen or air or oxygen enriched air, optionally in the presence of vapor and/or CO 2 ; reacting the mixture of reagents in the catalytic zone, at inlet temperatures ranging from 50 to 500° C. and space velocities ranging from 1,000 to 1,000,000 Nl reagents/L cat×h, reaching temperatures ranging from 450 to 1350° C.

Claims (9)

1. A process for the catalytic partial oxidation of liquid fuels, selected from low quality gas oils with a high content of aromatics and sulphur, together with gaseous fuels, selected from refinery gases, natural gas, and/or LPG, by means of a suitable catalytic system comprising the following steps:

premixing and optionally heating to temperatures ranging from 25 to 400° C. the reagents consisting of said liquid hydrocarbons, said gaseous hydrocarbons and oxygen or air or oxygen enriched air, optionally in the presence of vapour and/or CO 2 ;

reacting the mixture of reagents in the catalytic zone, at inlet temperatures ranging from 50 to 500° C. and space velocities ranging from 1000 to 1,000,000 Nl reagents/L cat×h, reaching temperatures at the outlet of the catalytic bed ranging from 450 to 1350° C.

2. The process according to claim 1 , wherein, heavy residues from oil distillation are also present among the reagents.

3. The process according to claim 2 , wherein the heavy residues from oil distillation are mixed with the reagents after being fluidized by means of thermal treatment or by dilution with suitable gas oils.

4. The process according to claim 1 , wherein the catalytic system consists of oxides, oxynitrides, nitrides, carbides and/or oxycarbides containing one or more elements selected from Rh, Ru, Ir, Pt, Ni, Fe, Co and Mo.

5. The process according to claim 1 , wherein, among the reagents, the ratio between vapour moles/moles of hydrocarbon carbon atoms at the inlet of the catalytic zone ranges from 0 to 2 and the ratio between oxygen moles/moles of hydrocarbon carbon atoms ranges from 0.1 to 0.8.

6. The process according to claim 1 , wherein, among the reagents, the ratio between vapour moles/moles of hydrocarbon carbon atoms at the inlet of the catalytic zone ranges from 0.1 to 1 and the ratio between oxygen moles/moles of hydrocarbon carbon atoms ranges from 0.25 to 0.75.

7. The process according to claim 1 , wherein low-quality gas oils with a high content of aromatics are selected from Light Cycle Oils (LCO) and Heavy Cycle Oils (HCO).

Assignments (3)
CORRECTIVE ASSIGNMENT TO CORRECT THE NAME OF THE ASSIGNOR PREVIOUSLY RECORDED ON REEL 023379 FRAME 0890. ASSIGNOR(S) HEREBY CONFIRMS THE CORPORATE MERGER. Recorded Nov 24, 2009
From: ENITECNOLOGIE S.P.A.
To: ENI S.P.A.
Reel/Frame 023556/0632 →
MERGER Recorded Oct 19, 2009
From: ENITECHNOLOGIE S.P.A.
To: ENI S.P.A.
Reel/Frame 023379/0890 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 18, 2008
From: BASINI, LUCA; BARTOLINI, ANDREA; LUPI, GIANCARLO; CLERICI, GABRIELE CARLO ETTORE
To: ENI S.P.A.; ENITECNOLOGIE S.P.A.
Reel/Frame 020663/0328 →