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US4332693A Expired / Lapsed US ⏱️ 0.0 years remaining

Agent for the purification of waste waters and process for its production

Assignee: Amcol International Corp
•
Filing: 1981-03-05
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Granted: 1982-06-01
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Expires: 2001-03-05
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Abstract

Abstract A chemical agent for treating oily emulsions and the like in industrial waste water includes a homogenous mixture of talc; adipic acid; aluminum sulfate; TIXOTON, a registered trademark; a flocculating agent; lime and bentonite. The process for producing the agent involves the steps of introducing the compounds, one at a time, and in the order listed above into a mixing chamber wherein the mixture is vigorously stirred until homogenity is achieved.

Inventors

  • 👤 Ralf F. Piepho

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 05:56
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/52; C02F1/5236; B; B01; B01D; B01D17/00; B01D17/02; B01D17/0202; B01D17/04; B01D17/047

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 87 words
A chemical agent for the treatment of contaminated waste waters, especially of waste waters in the form of oily emulsions, the agent being composed by weight of the following compounds in the following proportions: ______________________________________ Talc 1.5-2.5 kg Adipic Acid 2.0-3.0 kg Aluminum Sulfate 17.0-23.0 kg An acid activated bentonite, comprising approximately 56.7% SiO.sub.2 ; 20.2% Al.sub.2 O.sub.3 ; 2.9% CaO; 4.3% MgO; and 2.7% Na.sub.2 O + K.sub.2 O 35.0-48.0 kg A polymeric organic Flocculating Agent 0.3-0.5 kg Lime 12.0-15.0 kg Bentonite 20.0-28.0 kg 87.8-120.0 ______________________________________
Claim 2
Dependent Claim 87 words
A chemical agent for the treatment of contaminated waste waters, especially of waste waters in the form of oily emulsions, the agent being composed by weight of the following compounds in the following proportions: ______________________________________ Talc 1.5-2.5 kg Adipic Acid 2.0-3.0 kg Aluminum Sulfate 17.0-23.0 kg An acid activated bentonite, comprising approximately 56.7% SiO.sub.2 ; 20.2% Al.sub.2 O.sub.3 ; 2.9% CaO; 4.3% MgO; and 2.7% Na.sub.2 O + K.sub.2 O 35.0-48.0 kg A polymeric organic Flocculating Agent 0.3-0.5 kg Lime 12.0-15.0 kg Bentonite 20.0-28.0 kg 87.8-120.0 ______________________________________
Claim 3
Dependent Claim 14 words
The chemical agent as defined in claim 1 wherein the flocculating agent is polyacrylamide.
Claim 4
Dependent Claim 107 words
A chemical agent for the treatment of contaminated waste waters, especially of waste waters in the form of oily emulsions, wherein substantially 101 kg of the agent have the following composition by weight: ______________________________________ Talc 2 kg Adipic Acid 2.5 kg Aluminum Sulfate 20 kg A bentonite activated by contacting the bentonite with a mineral acid, heating the acid treated bentonite near 100° C. and removing excess acid, said activated bentonite comprising approximately 56.7% SiO.sub.2 ; 20.2% Al.sub.2 O.sub.3 ; 2.9% CaO; 4.3% MgO; and 2.7% Na.sub.2 O + K.sub.2 O 42 kg A polymeric organic Flocculating Agent 1 kg Lime 13.5 kg Bentonite 20 kg ______________________________________
Claim 5
Dependent Claim 107 words
A chemical agent for the treatment of contaminated waste waters, especially of waste waters in the form of oily emulsions, wherein substantially 101 kg of the agent have the following composition by weight: ______________________________________ Talc 2 kg Adipic Acid 2.5 kg Aluminum Sulfate 20 kg A bentonite activated by contacting the bentonite with a mineral acid, heating the acid treated bentonite near 100° C. and removing excess acid, said activated bentonite comprising approximately 56.7% SiO.sub.2 ; 20.2% Al.sub.2 O.sub.3 ; 2.9% CaO; 4.3% MgO; and 2.7% Na.sub.2 O + K.sub.2 O 42 kg A polymeric organic Flocculating Agent 1 kg Lime 13.5 kg Bentonite 20 kg ______________________________________
Claim 6
Dependent Claim 176 words
A process for the production of a chemical agent for the purification of waste waters, the chemical agent comprising talc, adipic acid, aluminum sulfate, a bentonite activated by contacting the bentonite with a mineral acid, heating the acid treated bentonite near 100° C. and removing excess acid, said activated bentonite comprising approximately 56.7% SiO 2 ; 20.0% Al 2 O 3 ; 2.9% CaO; 4.3% MgO; and 2.7% Na 2 O+K 2 O, a polymeric organic flocculating agent, lime and bentonite, the process including the steps of: (a) introducing the talc and the adipic acid and mixing them into an homogeneous mixture; (b) adding the aluminum sulfate to the talc-adipic acid mixture, and mixing until homogeneity is achieved; (c) adding said acid activated bentonite to the talc-adipic acid-aluminum sulfate mixture and mixing until homogeneity is achieved; (d) adding the polymeric organic flocculating agent to the talc-adipic acid-aluminum sulfate-acid activated bentonite mixture and mixing until homogeneity is achieved; (e) adding the lime to the talc-adipic acid-aluminum sulfate-acid activated bentonite-flocculating agent-lime mixture and mixing until homogeneity is acheived.
Claim 7
Dependent Claim 176 words
A process for the production of a chemical agent for the purification of waste waters, the chemical agent comprising talc, adipic acid, aluminum sulfate, a bentonite activated by contacting the bentonite with a mineral acid, heating the acid treated bentonite near 100° C. and removing excess acid, said activated bentonite comprising approximately 56.7% SiO 2 ; 20.0% Al 2 O 3 ; 2.9% CaO; 4.3% MgO; and 2.7% Na 2 O+K 2 O, a polymeric organic flocculating agent, lime and bentonite, the process including the steps of: (a) introducing the talc and the adipic acid and mixing them into an homogeneous mixture; (b) adding the aluminum sulfate to the talc-adipic acid mixture, and mixing until homogeneity is achieved; (c) adding said acid activated bentonite to the talc-adipic acid-aluminum sulfate mixture and mixing until homogeneity is achieved; (d) adding the polymeric organic flocculating agent to the talc-adipic acid-aluminum sulfate-acid activated bentonite mixture and mixing until homogeneity is achieved; (e) adding the lime to the talc-adipic acid-aluminum sulfate-acid activated bentonite-flocculating agent-lime mixture and mixing until homogeneity is acheived.
Claim 8
Dependent Claim 11 words
The process of claim 4 wherein the flocculating agent is polyacrylamide.
Claim 9
Dependent Claim 106 words
A chemical agent for the treatment of contaminated waste waters, especially of waste waters in the form of oily emulsions, the agent being composed by weight of the following compounds in the following proportions: ______________________________________ Talc 1.5-2.5 kg Adipic Acid 2.0-3.0 kg Aluminum Sulfate 17.0-23.0 kg A bentonite activated by contacting the bentonite with a mineral acid, heating the acid treated bentonite and removing excess acid, said activated bentonite comprising approximately 56.7% SiO.sub.2 ; 20.2% Al.sub.2 O.sub.3 ; 2.9% CaO; 4.3% MgO; and 2.7% Na.sub.2 O + K.sub.2 O 42 kg A polymeric organic Flocculating Agent 0.3-0.5 kg Lime 12.0-15.0 kg Bentonite 20.0-28.0 kg 87.8-120.0 ______________________________________
Claim 10
Dependent Claim 106 words
A chemical agent for the treatment of contaminated waste waters, especially of waste waters in the form of oily emulsions, the agent being composed by weight of the following compounds in the following proportions: ______________________________________ Talc 1.5-2.5 kg Adipic Acid 2.0-3.0 kg Aluminum Sulfate 17.0-23.0 kg A bentonite activated by contacting the bentonite with a mineral acid, heating the acid treated bentonite and removing excess acid, said activated bentonite comprising approximately 56.7% SiO.sub.2 ; 20.2% Al.sub.2 O.sub.3 ; 2.9% CaO; 4.3% MgO; and 2.7% Na.sub.2 O + K.sub.2 O 42 kg A polymeric organic Flocculating Agent 0.3-0.5 kg Lime 12.0-15.0 kg Bentonite 20.0-28.0 kg 87.8-120.0 ______________________________________

References Cited (Backward Citations)

US3428558A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-05-31 1985-11-30 1986-06-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-05-31 1989-11-30 1990-06-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-05-31 1993-11-30 1994-06-01 $7700.00 Window Closed / Lapsed

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