← Back to Patent Explorer
US4384878A Expired / Lapsed US ⏱️ 0.0 years remaining

Method and apparatus for composting compostable organic materials such as organic wastes and strongly aqueous fossile materials

Assignee: Armerad Betong Vagforbattringar AB
•
Filing: 1982-04-26
•
Granted: 1983-05-24
•
Expires: 2002-04-26
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract In a method of continuously composting material capable of being composted by the action of aerobic microorganisms in a reactor, the material is caused to pass through the reactor as a single mass from the top thereof to the bottom thereof from an upper level in said reactor, and in which oxygen-containing gas required for the aerobic decomposition of the compostable material is passed through said single mass in contact therewith. The waste gas from the composting process is removed from the reactor by suction through pipes which extend down into the mass to be composted from the upper level thereof, with the openings of said pipes lying on a level located beneath said upper level in said reactor. A pressure is maintained in said pipes of such magnitude as to cause oxygen-containing gas to pass from said upper level of the reactor through the layer of compostable material extending down to the openings of said tubes, said addition of oxygen-containing gas to the compostable material being intended to start the decomposition process.

Inventors

  • 👤 Tore Nordlund
  • 👤 Lars Ljungkvist

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 02:04
CPC Classifications
C; C05; C05F; C05F17/00; C05F17/90; C05F17/95; Y; Y02; Y02P; Y02P20/00; Y02P20/141; Y02P20/145; Y02W; Y02W30/00; Y02W30/40; Y10; Y10S; Y10S435/00; Y10S435/813

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 294 words
A method of continuously composting material capable of being composted by the action of aerobic microorganisms in a reactor, said method comprising the steps of: (a) introducing said material into the upper portion of said reactor, passing the material downwardly through said reactor, and collecting the material as a mass having an upper layer located below the upper level of the reactor, said material and mass continuously flowing from the top portion of said reactor to the bottom of said reactor; and (b) passing a major portion of the oxygen-containing gas required for aerobic decomposition of the compostable material countercurrently through said continuously flowing mass and in contact therewith, and maintaining reactor conditions such that composting of the mass is effected; (c) removing substantially all waste gas produced by said composting process from said reactor by suction through pipes which extend down into said mass from the upper level in said reactor, the openings of said pipes being arranged slightly below the upper layer of said mass at a level located beneath said upper level in said reactor; and (d) drawing through the upper level of said reactor concurrent to the flow of the mass, a minor portion of oxygen-containing gas; (e) maintaining simultaneously with said removing step, adequate negative pressure in said pipes as to cause the supplemental and minor portion of oxygen-containing gas, which has been introduced into said reactor, to pass from said upper level in said reactor, through the upper layer of said mass into which said pipes extend downwardly, and to said openings of said pipes, said passing of oxygen-containing gas from said upper level through said layer of said mass both starting the decomposition process and providing oxygen-containing gas to the composting area requiring the most oxygen-containing gas.
Claim 2
Independent Claim 294 words
A method of continuously composting material capable of being composted by the action of aerobic microorganisms in a reactor, said method comprising the steps of: (a) introducing said material into the upper portion of said reactor, passing the material downwardly through said reactor, and collecting the material as a mass having an upper layer located below the upper level of the reactor, said material and mass continuously flowing from the top portion of said reactor to the bottom of said reactor; and (b) passing a major portion of the oxygen-containing gas required for aerobic decomposition of the compostable material countercurrently through said continuously flowing mass and in contact therewith, and maintaining reactor conditions such that composting of the mass is effected; (c) removing substantially all waste gas produced by said composting process from said reactor by suction through pipes which extend down into said mass from the upper level in said reactor, the openings of said pipes being arranged slightly below the upper layer of said mass at a level located beneath said upper level in said reactor; and (d) drawing through the upper level of said reactor concurrent to the flow of the mass, a minor portion of oxygen-containing gas; (e) maintaining simultaneously with said removing step, adequate negative pressure in said pipes as to cause the supplemental and minor portion of oxygen-containing gas, which has been introduced into said reactor, to pass from said upper level in said reactor, through the upper layer of said mass into which said pipes extend downwardly, and to said openings of said pipes, said passing of oxygen-containing gas from said upper level through said layer of said mass both starting the decomposition process and providing oxygen-containing gas to the composting area requiring the most oxygen-containing gas.
Claim 3
Dependent Claim 14 words
A method as set forth in claim 1 wherein the oxygen-containing gas is air.
Claim 4
Dependent Claim 75 words
A method as set forth in claim 1 or 2, wherein the waste gas removed by suction from the composting process is caused to pass through a constriction in the pipes, said constriction producing a resistance to the flow of gas that is great as compared with the resistance of gas in the single mass between the upper level and the lower end of the pipes, thereby to compensate for any differences in gas resistance.

References Cited (Backward Citations)

US2474833A Cited
US3960537A Cited
US4062770A Cited
DE2709715A1 Cited
DE2721349A1 Cited
US4184269A Cited
US4203755A Cited
US4236910A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-05-23 1986-11-22 1987-05-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-05-23 1990-11-22 1991-05-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-05-23 1994-11-22 1995-05-24 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag