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US4047891A Expired / Lapsed US ⏱️ 0.0 years remaining

Density control system

Assignee: Combustion Engineering Inc
•
Filing: 1976-04-21
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Granted: 1977-09-13
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Expires: 1996-04-21
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Abstract

Abstract An air quality control system scrubs flue gas of SO 2 and particulates with a slurry of lime/limestone and water. The system includes a tank below the contact of gas and slurry in which the chemical action is completed and from which the slurry is recirculated to the scrubber. A bubbler system is connected to the reaction tank to detect the density of the slurry and monitor or control the density. The bubbler system is supplied the liquid and dissolved solids decanted from the thickener to which the slurry is drawn for disposal.

Inventors

  • 👤 Adolph August Schuetz

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 21:20
CPC Classifications
G; G01; G01N; G01N9/00; G01N9/26; G01N9/28; B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 99 words
A method of manifesting the percent undissolved solids in a mixture of finely divided undissolved solids and liquid with dissolved solids, including, establishing a collection of a mixture of finely divided undissolved solids and a first liquid with dissolved solids, injecting a second liquid with only dissolved solids equivalent to the dissolved solids of the mixture at two different elevations in the collected mixture, sensing the differential between the pressures required to inject the second liquid at the two different elevations, and manifesting the differential pressures as the density of the mixture and percent undissolved solids in the mixture.
Claim 2
Independent Claim 99 words
A method of manifesting the percent undissolved solids in a mixture of finely divided undissolved solids and liquid with dissolved solids, including, establishing a collection of a mixture of finely divided undissolved solids and a first liquid with dissolved solids, injecting a second liquid with only dissolved solids equivalent to the dissolved solids of the mixture at two different elevations in the collected mixture, sensing the differential between the pressures required to inject the second liquid at the two different elevations, and manifesting the differential pressures as the density of the mixture and percent undissolved solids in the mixture.
Claim 3
Dependent Claim 39 words
The method of claim 1, including, establishing a control signal with the differential pressures, and applying the control signal to vary the supply of finely divided undissolved solids to maintain the density of the mixture at a predetermined value.
Claim 4
Dependent Claim 52 words
The method of claim 2, in which, the undissolved solids is milled lime/limestone to be used for removing undesirable constituents from combustion gases, the dissolved solids are chemical species like calcium, sulfate, sulfite and magnesium ions, and the second liquid is injected in the collected mixture through a dual bubbler pipe system.
Claim 5
Dependent Claim 194 words
A control system for the density of a mixture of finely divided undissolved solids and liquids with dissolved solids, including, a means for combining finely divided undissolved solids and a first liquid with dissolved solids into a mixture, a tank through which the mixture is passed and in which the mixture is maintained at a predetermined level, a dual bubbler system with two pipes extended into the mixture within the tank, the open end of each pipe terminating at a different elevation below the surface of the mixture, a supply of a second liquid with only dissolved solids equivalent to the dissolved solids of the mixture connected to flow the liquid into the bubbler system and discharge from the open ends of each pipe to establish different pressures in each pipe, a differential pressure cell connected to the two pipes to generate a signal representative of the difference between the pressures of the second liquid in the two pipes, and means for applying the differential pressure signal to control the means regulating the density of the mixture of undissolved solids and liquid passed through the tank to maintain the mixture at a predetermined density.
Claim 6
Dependent Claim 194 words
A control system for the density of a mixture of finely divided undissolved solids and liquids with dissolved solids, including, a means for combining finely divided undissolved solids and a first liquid with dissolved solids into a mixture, a tank through which the mixture is passed and in which the mixture is maintained at a predetermined level, a dual bubbler system with two pipes extended into the mixture within the tank, the open end of each pipe terminating at a different elevation below the surface of the mixture, a supply of a second liquid with only dissolved solids equivalent to the dissolved solids of the mixture connected to flow the liquid into the bubbler system and discharge from the open ends of each pipe to establish different pressures in each pipe, a differential pressure cell connected to the two pipes to generate a signal representative of the difference between the pressures of the second liquid in the two pipes, and means for applying the differential pressure signal to control the means regulating the density of the mixture of undissolved solids and liquid passed through the tank to maintain the mixture at a predetermined density.
Claim 7
Dependent Claim 64 words
The system of claim 4 in which, the undissolved solids are lime/limestone applied to remove undesirable constituents from combustion gases, the dissolved solids are chemical species like calcium, sulfate, sulfite and magesium ions, and the supply of second liquid is liquid separated from the undissolved solids of the mixture after the mixture has been flowed from the tank and connected to the bubbler system.

References Cited (Backward Citations)

US3433057A Cited
US3897540A Cited
US3989465A Cited
US3904370A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-09-12 1981-03-14 1981-09-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-09-12 1985-03-14 1985-09-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-09-12 1989-03-14 1989-09-13 $7700.00 Window Closed / Lapsed

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