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US3674649A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for the production of humic acids, humates, and of compositions wherein they are contained

Assignee: I C B SpA IND CHIMICA E BIOLOG
•
Filing: 1969-05-19
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Granted: 1972-07-04
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Expires: 1989-05-19
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Abstract

Abstract Process for the preparation of humic acids and salts thereof by successive steps of fermentation of garbage and agricultural byproducts, under selected, controlled, temperature, time, and aeration conditions.

Inventors

  • 👤 Mario Formisano
  • 👤 Salvatore Coppola

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 19:08
CPC Classifications
C; C05; C05F; C05F11/00; C05F17/00; C05F17/20; C05F17/50; Y; Y02; Y02P; Y02P20/00; Y02P20/141; Y02P20/145; Y02W; Y02W30/00; Y02W30/40; Y10; Y10S; Y10S435/00; Y10S435/8215; Y10S435/822; Y10S435/831; Y10S435/886; Y10S435/911; Y10S435/913; Y10S435/916; Y10S435/917; Y10S435/933

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 25 words
A method according to claim 1, wherein the step (a) of exothermic fermentation is discontinued when the temperature is reduced down to its initial value.
Claim 2
Dependent Claim 43 words
A method according to claim 1, wherein the material is integrated, before being submitted to fermentation step (c), with the required mixture of mineral salts, selected from those which represent energetic and plastic substances for the growth of germs useful for the method.
Claim 3
Dependent Claim 37 words
A method according to claim 1, wherein mineral or organic substances, capable of stimulating the growth and metabolism of germs useful for the method, are added to the material, before it is submitted to fermentation step (c).
Claim 4
Dependent Claim 34 words
A method according to claim 1, wherein a quantity in thE range of 1-5 percent of siliceous materials is added to material that is being processed, before it is submitted to fermentation step (c).
Claim 5
Dependent Claim 30 words
A method according to claim 1 wherein the waste material is crushed until it contains not less than 10 percent of fine powder before being submitted to fermentation step (c).
Claim 6
Dependent Claim 21 words
A method according to claim 6 wherein the moisture contents is increased, simultaneously with the crushing operation, up to 40-50 percent.
Claim 7
Dependent Claim 17 words
A method according to claim 1 wherein the dilute acid in fermentation step (c) is dilute H2SO4.
Claim 8
Dependent Claim 23 words
A method according to claim 1, wherein a 30 percent solution of NaOH is utilized as concentrated alkali in the fermentation step (d).
Claim 9
Dependent Claim 26 words
A method according to claim 1, wherein the extraction step (f) is carried out with alkali having a normality in the range of N/5 and N/15.
Claim 10
Dependent Claim 29 words
A method according to claim 1 wherein extraction step (f) is carried out with an aqueous solution of middle concentration of an alkali salt of a weak organic acid.
Claim 11
Dependent Claim 19 words
A method as claimed in claim 1, wherein after the filtering of step (g) the humic acids are salified.
Claim 12
Dependent Claim 31 words
A method according to claim 12 wherein the salifying of humic acids is carried out with a hydroxide selected from the group consisting of potassium hydroxide, ammonium hydroxide, and calcium hydroxide.
Claim 13
Dependent Claim 49 words
A method according to claim 13, wherein the salifying may be carried out with alkali of those oligoelements which are essential to the physiology of plants, in view of their growing and of their destination for the human alimentation or livestock feeding, or even for pharmaceutical or phytotherapic applications.
Claim 14
Dependent Claim 29 words
A method according to claim 1, wherein the flocculation step (g) is carried out with organic or inorganic acids, down to a pH value in the range of 5-1.
Claim 15
Dependent Claim 39 words
A method according to claim 1 wherein a portion of the organic or inorganic acid used in flocculation step (g) at pH values in the range of 5-1 is bonded in a chemically stable form with a humic acids.
Claim 16
Dependent Claim 36 words
A method according to claim 16, wherein organic or inorganic acids, capable of increasing the fertilizing efficiency of the final products, or to develop a synergic action therewith, are utilized for the flocculation of humic acids.
Claim 17
Independent Claim 281 words
A method for the production of high yields of highly concentrated humic acids from waste materials selected from the group consisting of garbage, town refuse, byproducts of agriculture, and residues of other industrial fermentations, alone or mixed with each other and separated only from ferromagnetic materials, wherein said waste material is successively submitted to treatment steps comprising: a. an exothermic primary fermentation, controlled in particular by alternate aeration and stirring of the waste material, in order to promote the growth of micro-organisms in the range of natural epiphytic microflora naturally present in the waste material; b. an exothermic secondary fermentation, controlled by stirring and aeration in alternating cycles so that the temperature of the mass is about 20* C after about 2 weeks, thereby promoting the growth of said micro-organisms; c. treatment with dilute acid to a pH value of 5 + or - 0.5 and to a moisture content of 60-70 percent, followed by a fermentation with a massive culture of an eumycetic species selected from the group consisting of Gliocladium roseum, Popularia sphaerospherma, Aspergillus fumigatus, Sordaria fimicola, Mortiorella vinacea, Penicillium glacum, Aspergillus parasiticus, Aspergillus niger and Stisanus sp. at a temperature of 35*-37* C; d. treatment with concentrated alkali to a pH value of 7.0 + or - 0.2 and fermentation with a massive culture of Streptomyces nigrifaciens at a temperature of 28*-30* C; e. fermentation with a massive culture of AzotobacteR chroococcum at a temperature of 28*-30* C; f. extraction of humic acids from the thus treated waste material by means of dilute alkali; and g. flocculation of humic acids from the alkaline solution by the addition thereto of an acid up to the isoelectric point and filtering.
Claim 18
Independent Claim 262 words
A method for the production of high yields of highly concentrated humic acids from waste materials selected from the group consisting of garbage, town refuse, byproducts of agriculture, and residues of other industrial fermentations, alone or mixed with each other and separated only from ferromagnetic materials, wherein said waste material is successively submitted to treatment steps comprising: a. an exothermic primary fermentation, controlled in particular by alternate aeration and stirring of the waste material, in order to promote the growth of micro-organisms in the range of natural epiphytic microflora naturally present in the waste material; b. an exothermic secondary fermentation, controlled by stirring and aeration in alternating cycles so that the temperature of the mass is about 20* C after about 2 weeks, thereby promoting the growth of said micro-organisms; c. treatment with dilute acid to a pH value of 5 + or - 0.5 and to a moisture content of 60-70 percent, followed by a fermentation with a massive culture of Gliocladium catenulatum at a temperature of 35*-37* C; d. treatment with concentrated alkali to a pH value of 7.0 + or - 0.2 and fermentation with a massive culture of an actinomycetic, polyphenoloxydasic species, non-antagonistic of the Azotobacter chroococcum at a temperature of 28*-30* C; e. fermentation with a massive culture of Azotobacter chroococcum at a temperature of 28*-30* C; f. extraction of humic acids from the thus treated waste material by means of dilute alkali; and g. flocculation of humic acids from the alkaline solution by the addition thereto of an acid up to the isoelectric point and filtering.

References Cited (Backward Citations)

US3041157A Cited
US3142557A Cited
US3138448A Cited
US3235369A Cited
US3398186A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-07-04 1976-01-03 1976-07-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-07-04 1980-01-03 1980-07-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-07-04 1984-01-03 1984-07-04 $7700.00 Window Closed / Lapsed

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