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Patent · US4231868A · A · US

Process for dewatering mineral and coal concentrates

(11) Publication number
US4231868A
(21) Application number
US-113779-A
(22) Filing date
1979-01-05
(30) Priority date
1979-01-05
(43) Publication date
1980-11-04
(45) Date of grant
1980-11-04
(52) CPC
  • C22B Production and refining of metals; pretreatment of raw materials: 3/22
  • B01D Separation: 37/03
  • C02F Treatment of water, waste water, sewage, or sludge: 1/54
  • Y02P Climate change mitigation technologies in the production or processing of goods: 10/20
(73) Assignee
AMERICAN CYANAMID CO
(54) Title
Process for dewatering mineral and coal concentrates
(57) Abstract

Mineral and coal concentrates are effectively dewatered by a process wherein there is employed a dewatering aid comprising of an N-substituted sulfosuccinamate. The process provides for mixing the dewatering aid to an aqueous slurry of the concentrate and thereafter subjecting the treated slurry to filtration.

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Claims (8)

  1. A process for dewatering mineral and coal concentrates which comprises mixing with an aqueous slurry of the mineral or coal concentrate a dewatering aid in an amount ranging from about 0.15 pound per ton to about 5.0 pounds per ton, said dewatering aid consisting essentially of an N-monosubstituted sulfosuccinamate of the general structure: ##STR7## wherein R is a linear or branched aliphatic radical having four to fifteen carbon atoms, inclusive, R' is a linear or branched aliphatic radical having four to fifteen carbon atoms, inclusive, and X is hydrogen or a sulfonate salt, there being one X as hydrogen and one X as a sulfonate salt, and thereafter dewatering the treated slurry by filtration.
  2. The process of claim 1 wherein R is a linear or branched aliphatic radical having six to ten carbon atoms, inclusive.
  3. The process of claim 1 wherein R is 2-ethylhexyl.
  4. The process of claim 1 wherein R' is a linear or branched aliphatic radical having six to ten carbon atoms inclusive.
  5. The process of claim 1 wherein R' is n-octyl.
  6. The process of claim 1 wherein the dewatering aid dosage is from about 0.2 pound per ton to 1.0 pound per ton.
  7. The process of claim 1 wherein the dewatering aid employed is sodium N-octyl, 2-ethylhexyl sulfosuccinamate.
  8. The process of claim 1 wherein the dewatering aid employed is used in conjunction with nonionic surfactant, the total dosage of the dewatering aid and the nonionic surfactant within the range of from about 0.15 pounds per ton to about 5.0 pounds per ton.

Citations (9)

  • FR2079698A5
  • SU443682A1
  • US2252401A
  • US2266954A
  • US4097390A
  • US4107028A
  • US4146473A
  • US4153549A
  • US4156649A
Record as JSON
{
  "publication_number": "US4231868A",
  "country": "US",
  "kind": "A",
  "title": "Process for dewatering mineral and coal concentrates",
  "abstract": "Mineral and coal concentrates are effectively dewatered by a process wherein there is employed a dewatering aid comprising of an N-substituted sulfosuccinamate. The process provides for mixing the dewatering aid to an aqueous slurry of the concentrate and thereafter subjecting the treated slurry to filtration.",
  "claims": [
    "1. A process for dewatering mineral and coal concentrates which comprises mixing with an aqueous slurry of the mineral or coal concentrate a dewatering aid in an amount ranging from about 0.15 pound per ton to about 5.0 pounds per ton, said dewatering aid consisting essentially of an N-monosubstituted sulfosuccinamate of the general structure: ##STR7## wherein R is a linear or branched aliphatic radical having four to fifteen carbon atoms, inclusive, R' is a linear or branched aliphatic radical having four to fifteen carbon atoms, inclusive, and X is hydrogen or a sulfonate salt, there being one X as hydrogen and one X as a sulfonate salt, and thereafter dewatering the treated slurry by filtration.",
    "2. The process of claim 1 wherein R is a linear or branched aliphatic radical having six to ten carbon atoms, inclusive.",
    "3. The process of claim 1 wherein R is 2-ethylhexyl.",
    "4. The process of claim 1 wherein R' is a linear or branched aliphatic radical having six to ten carbon atoms inclusive.",
    "5. The process of claim 1 wherein R' is n-octyl.",
    "6. The process of claim 1 wherein the dewatering aid dosage is from about 0.2 pound per ton to 1.0 pound per ton.",
    "7. The process of claim 1 wherein the dewatering aid employed is sodium N-octyl, 2-ethylhexyl sulfosuccinamate.",
    "8. The process of claim 1 wherein the dewatering aid employed is used in conjunction with nonionic surfactant, the total dosage of the dewatering aid and the nonionic surfactant within the range of from about 0.15 pounds per ton to about 5.0 pounds per ton."
  ],
  "cpc": [
    "C22B 3/22",
    "B01D 37/03",
    "C02F 1/54",
    "Y02P 10/20"
  ],
  "assignees": [
    "AMERICAN CYANAMID CO"
  ],
  "filing_date": "1979-01-05",
  "publication_date": "1980-11-04",
  "grant_date": "1980-11-04",
  "priority_date": "1979-01-05",
  "application_number": "US-113779-A",
  "family_id": "21694566",
  "citations": [
    "FR2079698A5",
    "SU443682A1",
    "US2252401A",
    "US2266954A",
    "US4097390A",
    "US4107028A",
    "US4146473A",
    "US4153549A",
    "US4156649A"
  ]
}

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