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US3766971A Expired / Lapsed US ⏱️ 0.0 years remaining

Apparatus for removing pollutants from stack effluents

Assignee: Individual
•
Filing: 1971-05-13
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Granted: 1973-10-23
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Expires: 1991-05-13
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Abstract

Abstract A series of controlled gradient condensers for removing gaseous hydrocarbon pollutants from the stack effluent of an industrial treating plant, such as a veneer dryer. The gaseous effluent stream is conducted from the industrial treating plant to a precooler to bring the effluent temperature to the condensation point of the highest boiling pollutant. Thereafter the effluent stream is passed through a successive series of controlled gradient condenser, each operating in a temperature range lower than that of the immediately preceding condenser. The first several condensers are air cooled and designed to remove the higher boiling pollutants. Each air cooled condenser is wrapped with one or more heater coils, the turns of which are not uniformly wound about the condenser tubes but are more widely spaced toward the outlet or cold end of the condenser. Electric power to each heater coil is controlled by a respective power controller responsive to temperature sensors located inside the condenser for measuring a temperature gradient along the path of flow of the effluent. If any measured temperature gradient exceeds a predetermined maximum allowable limit, the power controller adjusts the electric power through the appropriate heater coil to restore the temperature gradient, and thus the cooling rate, to a value below the maximum limit. As long as the predetermined maximum temperature gradient or cooling rate for each gaseous pollutant is not exceeded the formation of aerosol is avoided and substantially all of the pollutant condenses in collectable liquid form on the walls of the condenser, thereby cleansing the effluent. Each condenser has a reservoir which collects the condensed pollutants by gravity feed, while the uncondensed remaining effluent passes to the next succeeding condenser. The last in the series of condensers is water cooled for condensing those pollutants having the lowest boiling points. The temperature gradient in the water cooled condenser is controlled by temperature sensors, similar to those in the air cooled condensers, which modulate the flow of coolant by controlling the power to the coolant pump. The different temperature ranges at which the respective condensers operate are preferably fixed so that the minimum temperature at the outlet of a respective condenser is greater than the highest melting point of any pollutant condensed within that condenser, so as to prevent solidification of the pollutants and fouling of the condensers. Immersion heaters in the condenser reservoirs further aid in preventing solidification. If solidification of one or more pollutants collected in a particular condenser cannot be avoided, scraper paddles are provided to scrape the solid material off the condenser walls for disposal through a solids removal port. The reservoir of the last in the series of condensers, from which the remaining effluent is vented to the atmosphere, includes a reservoir auxiliary cooling system for the purpose of further reducing effluent temperature if necessary to remove any remaining contaminants.

Inventors

  • 👤 E Baum

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 12:50
CPC Classifications
F; F28; F28B; F28B1/00; B; B01; B01D; B01D51/00; B01D51/10; F28B11/00; F28B7/00; Y; Y02; Y02A; Y02A50/00; Y02A50/20; Y02A50/2351

Claims Analysis

Total Claims: 21
Claim 1
Independent Claim 81 words
A method of removing components from a stream of gaseous effluent which comprises: a. gradually extracting heat from the effluent by cooling the effluent through the boiling points of the various components to be removed, thereby condensing the components; b. monitoring the amount of said components condensed in the form of aerosol; and c. reducing the rate at which heat is extracted from the effluent whenever the amount of said components condensed in the form of aerosol exceeds a predetermined limit.
Claim 2
Independent Claim 81 words
A method of removing components from a stream of gaseous effluent which comprises: a. gradually extracting heat from the effluent by cooling the effluent through the boiling points of the various components to be removed, thereby condensing the components; b. monitoring the amount of said components condensed in the form of aerosol; and c. reducing the rate at which heat is extracted from the effluent whenever the amount of said components condensed in the form of aerosol exceeds a predetermined limit.
Claim 3
Independent Claim 75 words
A method of removing a component from a stream of gaseous effluent by gradually cooling the stream and liquefying the component which comprises: a. determining a maximum rate of cooling for the stream above which the amount of aerosol formed in said stream by said cooling exceeds a predetermined limit; and b. gradually cooling said stream through the boiling point of said component at a controlled rate of cooling within said maximum rate of cooling.
Claim 4
Independent Claim 75 words
A method of removing a component from a stream of gaseous effluent by gradually cooling the stream and liquefying the component which comprises: a. determining a maximum rate of cooling for the stream above which the amount of aerosol formed in said stream by said cooling exceeds a predetermined limit; and b. gradually cooling said stream through the boiling point of said component at a controlled rate of cooling within said maximum rate of cooling.
Claim 5
Dependent Claim 44 words
The method of claim 2, wherein the cooling step (b) comprises: measuring the rate at which said effluent stream is being cooled; and reducing the rate at which said effluent stream is cooled when the measured cooling rate exceeds said predetermined maximum cooling rate.
Claim 6
Dependent Claim 29 words
The method of claim 2, further comprising: precooling the stream of effluent in advance of cooling step (b) down to the boiling point of the highest boiling component therein.
Claim 7
Dependent Claim 38 words
The method of claim 2, further comprising: measuring the concentration of said component in the effluent after the cooling step (b); and further cooling said effluent stream if such component concentration is in excess of a predetermined limit.
Claim 8
Independent Claim 84 words
A method of removing pollutants from a stream of gaseous stack effluent before such effluent is vented to the atmosphere which comprises: a. gradually cooling the effluent stream through the boiling points of the various pollutants to be removed, thereby condensing and separating such pollutants from said effluent; b. measuring the pollutant concentration in the effluent after such cooling step; c. further cooling said effluent stream prior to venting it to the atmosphere if such pollutant concentration is in excess of a predetermined limit.
Claim 9
Independent Claim 84 words
A method of removing pollutants from a stream of gaseous stack effluent before such effluent is vented to the atmosphere which comprises: a. gradually cooling the effluent stream through the boiling points of the various pollutants to be removed, thereby condensing and separating such pollutants from said effluent; b. measuring the pollutant concentration in the effluent after such cooling step; c. further cooling said effluent stream prior to venting it to the atmosphere if such pollutant concentration is in excess of a predetermined limit.
Claim 10
Independent Claim 107 words
A method of removing pollutants from the gaseous stack effluent of an industrial treating plant, said pollutants having different boiling and melting points and a first one of said pollutants having a boiling point and a melting point higher than the boiling point of a second one of said pollutants, which method comprises: a. cooling said effluent to the boiling point of said first pollutant to liquefy said first pollutant; b. further cooling said effluent toward the boiling point of said second pollutant; c. removing said first pollutant from said effluent in liquid form before said effluent is cooled to the boiling point of said second pollutant.
Claim 11
Independent Claim 107 words
A method of removing pollutants from the gaseous stack effluent of an industrial treating plant, said pollutants having different boiling and melting points and a first one of said pollutants having a boiling point and a melting point higher than the boiling point of a second one of said pollutants, which method comprises: a. cooling said effluent to the boiling point of said first pollutant to liquefy said first pollutant; b. further cooling said effluent toward the boiling point of said second pollutant; c. removing said first pollutant from said effluent in liquid form before said effluent is cooled to the boiling point of said second pollutant.
Claim 12
Dependent Claim 27 words
The method of claim 7 wherein said first pollutant is reMoved from said effluent before said effluent is cooled to the melting point of said first pollutant.
Claim 13
Dependent Claim 48 words
The method of claim 1 wherein said cooling step (a) is accomplished by passing said effluent stream through a condenser, and wherein said cooling rate reduction step (c) is accomplished by emitting heat adjacent said gaseous effluent stream to counteract the cooling of said stream by said condenser.
Claim 14
Dependent Claim 46 words
The method of claim 9, further comprising exposing a piezoelectric oscillator to said effluent stream for measuring an aerosol count rate in said stream and utilizing said piezoelectric oscillator to generate an emf in proportion to said count rate for controlling the emission of said heat.
Claim 15
Dependent Claim 44 words
The method of claim 2 wherein said cooling step (b) is accomplished by passing said stream through a condenser and wherein said rate of cooling is controlled by emitting heat adjacent to said stream to counteract the cooling of said stream by said condenser.
Claim 16
Dependent Claim 54 words
The method of claim 11 wherein a greater concentration of heat is emitted toward the upstream end of said condenser where said effluent stream enters than toward the downstream end, so as to cause a reduction in cooling rate which is greater toward the upstream end than toward the downstream end of said condenser.
Claim 17
Dependent Claim 50 words
The method of claim 2 wherein said cooling step (b) is accomplished by passing said stream through a condenser of the type which cools said effluent stream by means of a flow of coolant, and wherein said cooling rate is controlled by controlling the rate of flow of said coolant.
Claim 18
Dependent Claim 36 words
The method of claim 2, further comprising preheating the stream of effluent in advance of cooling step (b) to maintain the temperature of said stream at substantially the boiling point of the highest boiling component therein.
Claim 19
Dependent Claim 50 words
The method of claim 3 wherein the rate at which said effluent stream is cooled is measured by means of a pair of temperature sensors located a spaced distance apart along the path of flow of said stream to measure the temperature differential of said stream between said temperature sensors.
Claim 20
Dependent Claim 32 words
The method of claim 7 including the step of supplying heat to said first pollutant after it has been removed from said effluent so as to prevent solidification of said first pollutant.
Claim 21
Dependent Claim 66 words
The method of claim 7 wherein said effluent is cooled by passing it through a condenser and wherein said first pollutant is removed from said effluent by collecting it in a reservoir located at a point along the path of travel of said effluent through said condenser in advance of the point where said condenser cools said effluent to the melting point of said first pollutant.

References Cited (Backward Citations)

US3589169A Cited
US3651686A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-10-22 1977-04-23 1977-10-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-10-22 1981-04-23 1981-10-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-10-22 1985-04-23 1985-10-23 $7700.00 Window Closed / Lapsed

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