US4046522A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Pre-engine converter for use with fuels containing oxygenated compounds
Assignee: Mobil Oil AS
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Filing: 1976-06-25
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Granted: 1977-09-06
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Expires: 1996-06-25
Abstract
Abstract A pre-engine catalytic converter for use with fuels which are mixtures of hydrocarbons and oxygenated organic compounds, such as alcohols, ethers and ketones, convertible to carbon monoxide and H 2 . The converter comprises two catalyst beds arranged in series, the first containing a catalyst suitable for the decomposition of organic oxygenates to CO and H 2 and the second containing a cracking catalyst of the ZSM-5 zeolite type to convert the liquid hydrocarbon fuel to gaseous hydrocarbon fuel. Energy is extracted from the engine exhaust by heat exchange and utilized to support the catalytic reactions whereby the heating value and the octane rating of the fuel are increased. The performance and fuel economy of the engine are substantially improved.
Inventors
- 👤 Nai Yuen Chen
- 👤 Heinz Heinemann
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 07:12
CPC Classifications
C; C10; C10G; C10G11/00; C10G11/02; C10G11/04; C10G11/05; C01; C01B; C01B3/00; C01B3/02; C01B3/22; C01B3/32; C01B3/34; C01B3/38
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
265 words
A pre-engine converter comprising: a. two sequential reaction chambers; b. a catalytic material in the first of said chambers that is effective to catalytically decompose oxygen-containing organic compounds to carbon monoxide and hydrogen; c. a catalytic material in the second of said chambers that comprises a crystalline aluminosilicate zeolite having a silica to alumina ratio of at least 12, a constraint index of 1 to 12, and a crystal density of not substantially below about 1.6 grams per cubic centimeter and is effective for catalytically cracking low octane normally liquid hydrocarbons to higher octane normally gaseous hydrocarbons; d. means for introducing into said first chamber a liquid fuel comprising a low octane normally liquid hydrocarbon in mixture with one or more low molecular weight, high octane value, oxygen-containing organic compounds; e. means for passing the effluent from said first chamber into said second chamber; f. means for removing from said second chamber an effluent comprising carbon monoxide, hydrogen and higher octane normally gaseous hydrocarbons; g. means for mixing air with the gaseous effluent from said second chamber; h. means to introduce into an internal combustion engine the mixture of air and said gaseous effluent; i. means to pass the hot exhaust gases from said engine into indirect heat exchange relationship with said pre-engine converter; j. means enclosing said first and second reaction chambers and connected to said exhaust means whereby the heat from said hot exhaust gases emitting from said engine is transferred to said reaction chambers and the catalysts contained therein; and k. means for venting said exhaust gases from said heat transfer means.
Claim 2
Dependent Claim
265 words
A pre-engine converter comprising: a. two sequential reaction chambers; b. a catalytic material in the first of said chambers that is effective to catalytically decompose oxygen-containing organic compounds to carbon monoxide and hydrogen; c. a catalytic material in the second of said chambers that comprises a crystalline aluminosilicate zeolite having a silica to alumina ratio of at least 12, a constraint index of 1 to 12, and a crystal density of not substantially below about 1.6 grams per cubic centimeter and is effective for catalytically cracking low octane normally liquid hydrocarbons to higher octane normally gaseous hydrocarbons; d. means for introducing into said first chamber a liquid fuel comprising a low octane normally liquid hydrocarbon in mixture with one or more low molecular weight, high octane value, oxygen-containing organic compounds; e. means for passing the effluent from said first chamber into said second chamber; f. means for removing from said second chamber an effluent comprising carbon monoxide, hydrogen and higher octane normally gaseous hydrocarbons; g. means for mixing air with the gaseous effluent from said second chamber; h. means to introduce into an internal combustion engine the mixture of air and said gaseous effluent; i. means to pass the hot exhaust gases from said engine into indirect heat exchange relationship with said pre-engine converter; j. means enclosing said first and second reaction chambers and connected to said exhaust means whereby the heat from said hot exhaust gases emitting from said engine is transferred to said reaction chambers and the catalysts contained therein; and k. means for venting said exhaust gases from said heat transfer means.
Claim 3
Dependent Claim
20 words
The pre-engine converter of claim 1 wherein the catalyst in each of the two chambers is a solid, particulate material.
Claim 4
Dependent Claim
13 words
The pre-engine converter of claim 1 wherein the zeolite cracking catalyst is ZSM-5.
Claim 5
Dependent Claim
241 words
In the operation of an internal combustion engine, the process of converting in a pre-engine converter used in conjunction with such engine a liquid fuel feed mixture comprising low octane, normally liquid hydrocarbons and one or more low molecular weight, low heating value, oxygen-containing organic compounds, said mixture being suitable for intermittent cold operation of said engine, to a higher octane, higher heating value gaseous fuel comprising normally gaseous hydrocarbons, carbon monoxide and hydrogen, which process comprises: a. heating said pre-engine converter by passing the hot exhaust gases from said engine in indirect heat exchange relationship therewith; b. initially contacting said liquid fuel mixture with a catalytic material suitable for the decomposition of oxygen-containing organic compounds, c. which catalytic material decomposes the oxygen-containing organic compounds in the normally liquid fuel feed mixture to carbon monoxide and hydrogen; d. then contacting the effluent therefrom with a second catalyst comprising a crystalline aluminosilicate zeolite cracking catalyst having a silica to alumina ratio of at least 12, a constraint index of 1 to 12 and a crystal density of not substantially below about 1.6 grams per cubic centimeter; e. whereby the low octane normally liquid hydrocarbons of the feed mixture are converted to higher octane normally gaseous hydrocarbons and provide, as an effluent from said contact with said cracking catalyst, a fuel mixture comprising CO, H 2 and gaseous hydrocarbons having higher octane value and higher heating value than said liquid fuel feed mixture.
Claim 6
Dependent Claim
241 words
In the operation of an internal combustion engine, the process of converting in a pre-engine converter used in conjunction with such engine a liquid fuel feed mixture comprising low octane, normally liquid hydrocarbons and one or more low molecular weight, low heating value, oxygen-containing organic compounds, said mixture being suitable for intermittent cold operation of said engine, to a higher octane, higher heating value gaseous fuel comprising normally gaseous hydrocarbons, carbon monoxide and hydrogen, which process comprises: a. heating said pre-engine converter by passing the hot exhaust gases from said engine in indirect heat exchange relationship therewith; b. initially contacting said liquid fuel mixture with a catalytic material suitable for the decomposition of oxygen-containing organic compounds, c. which catalytic material decomposes the oxygen-containing organic compounds in the normally liquid fuel feed mixture to carbon monoxide and hydrogen; d. then contacting the effluent therefrom with a second catalyst comprising a crystalline aluminosilicate zeolite cracking catalyst having a silica to alumina ratio of at least 12, a constraint index of 1 to 12 and a crystal density of not substantially below about 1.6 grams per cubic centimeter; e. whereby the low octane normally liquid hydrocarbons of the feed mixture are converted to higher octane normally gaseous hydrocarbons and provide, as an effluent from said contact with said cracking catalyst, a fuel mixture comprising CO, H 2 and gaseous hydrocarbons having higher octane value and higher heating value than said liquid fuel feed mixture.
Claim 7
Dependent Claim
25 words
The process of claim 4 wherein said oxygen-containing organic compound is present in amounts greater than 2% by volume in said liquid fuel feed mixture.
Claim 8
Dependent Claim
12 words
The process of claim 4 wherein said oxygen-containing compound is methyl alcohol.
Claim 9
Dependent Claim
45 words
The process of claim 4 wherein water is added to said liquid fuel feed mixture in an amount according to the following equation: ##EQU3## where C a H b O is the empirical formula for said oxygen-containing organic compound and a ≧2 and b ≧6.
Claim 10
Dependent Claim
28 words
The process of claim 4 wherein said catalytic material for the decomposition of oxygen-containing organic compounds is alumina, zinc chromite, copper zinc chromite, manganese chromite, iron or cobalt.
Claim 11
Dependent Claim
12 words
The process in claim 4 wherein said zeolite cracking catalyst is ZSM-5.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-09-05 | 1981-03-07 | 1981-09-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-09-05 | 1985-03-07 | 1985-09-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-09-05 | 1989-03-07 | 1989-09-06 | $7700.00 | Window Closed / Lapsed |