Patent US3999959A successfully refreshed from Google Patents.
US3999959A
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US
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Motor fuel blending control system
Assignee: Universal Oil Products Co
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Filing: 1974-08-12
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Granted: 1976-12-28
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Expires: 1994-08-12
Abstract
Abstract At least two gasoline streams, having dissimilar octane ratings, are admixed with a butane-rich stream, the latter for vapor pressure control. A control system is employed to regulate the quantity of a lead-containing compound and/or the relative quantities of the blend components to achieve both the target octane of the final motor fuel blend as well as the desired vapor pressure, or volatility.
Inventors
- 👤 Walter A. Bajek
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 20:57
CPC Classifications
G; G01; G01N; G01N33/00; G01N33/26; G01N33/28; G01N33/2829; C; C10; C10L; C10L1/00; C10L1/04; C10L1/06; G05; G05D; G05D21/00; G05D21/02; Y; Y10; Y10S; Y10S44/00; Y10S44/903; Y10T; Y10T137/00; Y10T137/2496; Y10T137/2514; Y10T137/2521; Y10T137/2529; Y10T436/00; Y10T436/21; Y10T436/214
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
306 words
In a process for motor fuel blending, wherein two gasoline streams, having dissimilar octane ratings, are admixed and (i) a butane-rich stream is added for vapor pressure control, and (ii) a lead-containing compound is added to increase the octane rating of the motor fuel blend, the control system which comprises, in cooperative combination: a. first flow-varying means for adjusting the flow rate of the gasoline stream having the higher octane rating; b. second flow-varying means for adjusting the flow rate of the gasoline stream having the lower octane rating; c. third flow-varying means for adjusting the flow rate of said butane-rich stream; d. a first hydrocarbon analyzer receiving a sample of the blend of said butane stream, said higher octane gasoline stream and said lower octane stream, and developing a first output signal representative of a volatility characteristic of said sample; e. a second hydrocarbon analyzer receiving a second sample of said blend, and developing a second output signal representative of the octane rating of said sample; f. comparator means, receiving said first and second output signals, which compares the rate of change thereof and the actual value of the octane rating of said blend, and generates third and fourth output signals; g. fourth flow-varying means for adjusting the flow rate of said lead-containing compound added to said blend; h. first signal-receiving means to which said third output signal is transmitted by said comparator means, said first signal-receiving means in turn transmitting to said fourth flow-varying means, whereby the flow of said lead-containing compound is adjusted in response to said octane rating; and, i. second signal-receiving means to which said fourth output signal is transmitted by said comparator means, said second signal-receiving means in turn transmitting to said third flow-varying means whereby the flow of said butane stream is adjusted in response to said composition characteristic.
Claim 2
Dependent Claim
306 words
In a process for motor fuel blending, wherein two gasoline streams, having dissimilar octane ratings, are admixed and (i) a butane-rich stream is added for vapor pressure control, and (ii) a lead-containing compound is added to increase the octane rating of the motor fuel blend, the control system which comprises, in cooperative combination: a. first flow-varying means for adjusting the flow rate of the gasoline stream having the higher octane rating; b. second flow-varying means for adjusting the flow rate of the gasoline stream having the lower octane rating; c. third flow-varying means for adjusting the flow rate of said butane-rich stream; d. a first hydrocarbon analyzer receiving a sample of the blend of said butane stream, said higher octane gasoline stream and said lower octane stream, and developing a first output signal representative of a volatility characteristic of said sample; e. a second hydrocarbon analyzer receiving a second sample of said blend, and developing a second output signal representative of the octane rating of said sample; f. comparator means, receiving said first and second output signals, which compares the rate of change thereof and the actual value of the octane rating of said blend, and generates third and fourth output signals; g. fourth flow-varying means for adjusting the flow rate of said lead-containing compound added to said blend; h. first signal-receiving means to which said third output signal is transmitted by said comparator means, said first signal-receiving means in turn transmitting to said fourth flow-varying means, whereby the flow of said lead-containing compound is adjusted in response to said octane rating; and, i. second signal-receiving means to which said fourth output signal is transmitted by said comparator means, said second signal-receiving means in turn transmitting to said third flow-varying means whereby the flow of said butane stream is adjusted in response to said composition characteristic.
Claim 3
Dependent Claim
54 words
The control system of claim 1 further characterized in that said comparator means generates a fifth output signal which is transmitted to third signal-receiving means, said third signal-receiving means in turn transmitting to said first flow-varying means, whereby the flow of said higher octane gasoline stream is adjusted in response to said octane rating.
Claim 4
Dependent Claim
54 words
The control system of claim 1 further characterized in that said comparator means generates a sixth output signal which is transmitted to fourth signal-receiving means, said fourth signal-receiving means in turn transmitting to said second flow-varying means, whereby the flow of said lower octane gasoline stream is adjusted in response to said octane rating.
Claim 5
Dependent Claim
25 words
The control system of claim 1 further characterized in that said second hydrocarbon analyzer comprises a stabilized cool flame generator having a servo-positioned flame front.
Claim 6
Dependent Claim
23 words
The control system of claim 1 further characterized in that said first output signal is representative of the boiling point of said blend.
Claim 7
Dependent Claim
23 words
The control system of claim 1 further characterized in that said first output signal is representative of the vapor/liquid ratio of said sample.
Claim 8
Dependent Claim
263 words
A process for blending motor fuel which comprises the steps of: a. admixing a butane-rich stream with a first gasoline stream, having a relatively high octane rating, and a second gasoline stream, having a lower octane rating; b. regulating the flow rates of said first and second gasoline streams, and said butane-rich stream by adjusting first, second and third flow-varying means; c. introducing a first sample of the resulting motor fuel blend into a first hydrocarbon analyzer and developing therein a first output signal representative of a volatility characteristic of said sample; d. introducing a second sample of the resulting motor fuel blend into a second hydrocarbon analyzer and developing therein a second output signal representative of the octane rating thereof; e. transmitting said first and second output signals to comparator means, which compares the rate of change thereof and the actual value of the octane rating of said second sample, and generating therein third, fourth, fifth and sixth output signals; f. admixing a lead-containing compound with said motor fuel blend, regulating the flow of said compound by fourth flow-varying means; g. transmitting said third output signal to said fourth flow-varying means, whereby the flow of said lead-containing compound is adjusted in response to said octane rating; and, h. transmitting at least one of said fourth, fifth and sixth output signals to at least one of said first, second and third flow-varying means, whereby the flow of at least one of said first and second gasoline streams, and said butane-rich stream is adjusted in response to said octane rating, or said composition characteristic.
Claim 9
Dependent Claim
263 words
A process for blending motor fuel which comprises the steps of: a. admixing a butane-rich stream with a first gasoline stream, having a relatively high octane rating, and a second gasoline stream, having a lower octane rating; b. regulating the flow rates of said first and second gasoline streams, and said butane-rich stream by adjusting first, second and third flow-varying means; c. introducing a first sample of the resulting motor fuel blend into a first hydrocarbon analyzer and developing therein a first output signal representative of a volatility characteristic of said sample; d. introducing a second sample of the resulting motor fuel blend into a second hydrocarbon analyzer and developing therein a second output signal representative of the octane rating thereof; e. transmitting said first and second output signals to comparator means, which compares the rate of change thereof and the actual value of the octane rating of said second sample, and generating therein third, fourth, fifth and sixth output signals; f. admixing a lead-containing compound with said motor fuel blend, regulating the flow of said compound by fourth flow-varying means; g. transmitting said third output signal to said fourth flow-varying means, whereby the flow of said lead-containing compound is adjusted in response to said octane rating; and, h. transmitting at least one of said fourth, fifth and sixth output signals to at least one of said first, second and third flow-varying means, whereby the flow of at least one of said first and second gasoline streams, and said butane-rich stream is adjusted in response to said octane rating, or said composition characteristic.
Claim 10
Dependent Claim
22 words
The process of claim 7 further characterized in that said first output signal is representative of the boiling point of said blend.
Claim 11
Dependent Claim
22 words
The process of claim 7 further characterized in that said first output signal is representative of the vapor/liquid ratio of said blend.
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) | 1979-12-28 | 1980-06-28 | 1980-12-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-12-28 | 1984-06-28 | 1984-12-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-12-28 | 1988-06-28 | 1988-12-28 | $7700.00 | Window Closed / Lapsed |