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Patent · US4663859A · A · US

Method for improving strength of dry dye particles and reducing explosion hazards

(11) Publication number
US4663859A
(21) Application number
US-78412985-A
(22) Filing date
1985-10-04
(30) Priority date
1985-10-04
(43) Publication date
1987-05-12
(45) Date of grant
1987-05-12
(52) CPC
  • C09B Organic dyes or closely-related compounds for producing dyes {, e.g. pigments}; mordants; lakes: 67/0095, 67/0003
(73) Assignee
CIBA GEIGY CORP
(54) Title
Method for improving strength of dry dye particles and reducing explosion hazards
(57) Abstract

A process for preparing dry dye granules is disclosed. The process involves the preparation of a controlled moisture content slurry of the dye. Then introducing the slurry into a turbogranulator to form solid spherical particles whose size is controlled by the moisture content of the slurry. Then drying the particles in a fluidized bed dryer by heated air. Most of the fines are removed during the drying stage in the exit air stream from the dryer. The remaining fines and over sized particles are recovered on screening and are combined and ground and used to control the moisture content of the initial slurry. The final solid granules have good strength as compared to the previously marketed spray-dried materials which were in the form of porous hollow spheres. They are more readily dispersible and more rapidly dissolving.

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Claims (5)

  1. A process for the production of uniform, high strength granules of dyes which comprises the steps of forming a pumpable standardized slurry of the dye; feeding the slurry into a high-intensity turbine-type granulator; granulating said feed in the granulator between its turbine casing and its rotor elements; discharging the formed wet granules unto a fluidized-bed particulate dryer; drying said wet granules by a stream of dry heated air blown through the bed of granules in said dryer; said air stream, on leaving the bed entraining the fines of undersized granules which are then separated from said air stream; and discharging the remaining dry granules from said fluidized bed dryer.
  2. The process according to claim 1 wherein the dried granules discharged from the fluidized bed are sieved to separate any oversized granules.
  3. The process according to claim 1 wherein the dry fines separated from the air stream and/or the dried oversized granules, from claim 2, ground to powder, are combined and fed to the turbogranulator to standardize the moisture content granulator mix.
  4. The process according to claim 3 wherein the granulator mix is standardized to higher moisture content when the granules are undersized and the granulator mix is standardized to a lower moisture content when the granule particle size is to be reduced.
  5. Granules of dyestuffs prepared according to the process of claim 1.

Citations (3)

  • US3748745A
  • US3879855A
  • US4327998A
Record as JSON
{
  "publication_number": "US4663859A",
  "country": "US",
  "kind": "A",
  "title": "Method for improving strength of dry dye particles and reducing explosion hazards",
  "abstract": "A process for preparing dry dye granules is disclosed. The process involves the preparation of a controlled moisture content slurry of the dye. Then introducing the slurry into a turbogranulator to form solid spherical particles whose size is controlled by the moisture content of the slurry. Then drying the particles in a fluidized bed dryer by heated air. Most of the fines are removed during the drying stage in the exit air stream from the dryer. The remaining fines and over sized particles are recovered on screening and are combined and ground and used to control the moisture content of the initial slurry. The final solid granules have good strength as compared to the previously marketed spray-dried materials which were in the form of porous hollow spheres. They are more readily dispersible and more rapidly dissolving.",
  "claims": [
    "1. A process for the production of uniform, high strength granules of dyes which comprises the steps of forming a pumpable standardized slurry of the dye; feeding the slurry into a high-intensity turbine-type granulator; granulating said feed in the granulator between its turbine casing and its rotor elements; discharging the formed wet granules unto a fluidized-bed particulate dryer; drying said wet granules by a stream of dry heated air blown through the bed of granules in said dryer; said air stream, on leaving the bed entraining the fines of undersized granules which are then separated from said air stream; and discharging the remaining dry granules from said fluidized bed dryer.",
    "2. The process according to claim 1 wherein the dried granules discharged from the fluidized bed are sieved to separate any oversized granules.",
    "3. The process according to claim 1 wherein the dry fines separated from the air stream and/or the dried oversized granules, from claim 2, ground to powder, are combined and fed to the turbogranulator to standardize the moisture content granulator mix.",
    "4. The process according to claim 3 wherein the granulator mix is standardized to higher moisture content when the granules are undersized and the granulator mix is standardized to a lower moisture content when the granule particle size is to be reduced.",
    "5. Granules of dyestuffs prepared according to the process of claim 1."
  ],
  "cpc": [
    "C09B 67/0095",
    "C09B 67/0003"
  ],
  "assignees": [
    "CIBA GEIGY CORP"
  ],
  "filing_date": "1985-10-04",
  "publication_date": "1987-05-12",
  "grant_date": "1987-05-12",
  "priority_date": "1985-10-04",
  "application_number": "US-78412985-A",
  "family_id": "25131437",
  "citations": [
    "US3748745A",
    "US3879855A",
    "US4327998A"
  ]
}

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