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Patent · US4018671A · A · US

Intermittent catalyst addition system

(11) Publication number
US4018671A
(21) Application number
US-54371975-A
(22) Filing date
1975-01-14
(30) Priority date
1975-01-14
(43) Publication date
1977-04-19
(45) Date of grant
1977-04-19
(52) CPC
  • B01J Chemical or physical processes, e.g. catalysis or colloid chemistry; their relevant apparatus: 8/0015, 2208/00752, 8/0035
  • C10G Cracking hydrocarbon oils; production of liquid hydrocarbon mixtures, e.g. by destructive hydrogenation, oligomerisation, polymerisation; recovery of hydrocarbon oils from oil-shale, oil-sand, or gases; refining mixtures mainly consisting of hydrocarbons; reforming of naphtha; mineral waxes: 11/18, 11/187
(73) Assignee
MARATHON OIL CO
(54) Title
Intermittent catalyst addition system
(57) Abstract

Catalyst, e.g., for a fluid catalytic cracker, is added automatically by a system consisting of an addition hopper which is periodically fed by gravity from a storage hopper, sealed off from the supply, and then pressurized with air to discharge its contents to the carrier gas line feeding the hydrocarbon conversion unit, e.g., the regenerator section of a Fluid Catalytic Cracking Unit. Sequencing can be by electronic timer-solenoid (or pneumatic) valve system.

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Claims (6)

  1. In the catalytic conversion of feed materials by contacting said feed materials in a converter system with catalyst in a fluidized state, some of which catalyst is lost from said catalytic cracking process through reduced activity and/or entrainment in the effluent from said process, the improvement comprising: a. storing said catalyst in a storage tank maintained at a first internal pressure and having a conduit communicating through a storage valve with an addition hopper; b. maintaining said addition hopper at a pressure corresponding substantially to said first pressure of said storage tank by operation of a venting means and opening said storage valve to admit said catalyst to a predetermined level in said addition hopper, said addition hopper communicating through an addition valve to a carrier gas line leading to said converter; c. closing said venting means and pressurizing said addition hopper to a second addition pressure; d. thereafter opening said addition valve and permitting said addition hopper to empty into said carrier gas line; e. after emptying of said addition hopper, closing said addition valve, opening said venting means to reduce the pressure in said addition hopper to said first pressure, and opening said storage valve to admit additional catalyst to fill said addition hopper to a predetermined level determined by the volume of said addition hopper; f. thereafter closing said venting means, closing said storage valve and admitting additional gases to raise the pressure of said addition hopper to said addition pressure; g. thereafter opening said addition valve to admit additional catalyst to said carrier gas line and repeating the above cycle.
  2. A process according to claim 1 wherein the duration of opening of each of said valves is controlled by timing means.
  3. A process according to claim 2 wherein the position of each of said valves is controlled by a sequencing control center.
  4. A process according to claim 1 wherein said addition valve is closed substantially whenever said storage valve is open and wherein said storage valve is closed substantially whenever said addition valve is open, and wherein said venting means is open whenever said storage valve is open and wherein said storage valve is closed whenever said venting means is closed.
  5. A process according to claim 4 wherein said venting means communicates with an upper portion of said catalyst storage tank.
  6. A process according to claim 1 wherein said storage tank has a first pressure of approximately atmospheric pressure.

Citations (7)

  • US1535991A
  • US2786800A
  • US2892773A
  • US3090593A
  • US3156537A
  • US3479093A
  • US3850582A
Record as JSON
{
  "publication_number": "US4018671A",
  "country": "US",
  "kind": "A",
  "title": "Intermittent catalyst addition system",
  "abstract": "Catalyst, e.g., for a fluid catalytic cracker, is added automatically by a system consisting of an addition hopper which is periodically fed by gravity from a storage hopper, sealed off from the supply, and then pressurized with air to discharge its contents to the carrier gas line feeding the hydrocarbon conversion unit, e.g., the regenerator section of a Fluid Catalytic Cracking Unit. Sequencing can be by electronic timer-solenoid (or pneumatic) valve system.",
  "claims": [
    "1. In the catalytic conversion of feed materials by contacting said feed materials in a converter system with catalyst in a fluidized state, some of which catalyst is lost from said catalytic cracking process through reduced activity and/or entrainment in the effluent from said process, the improvement comprising: a. storing said catalyst in a storage tank maintained at a first internal pressure and having a conduit communicating through a storage valve with an addition hopper; b. maintaining said addition hopper at a pressure corresponding substantially to said first pressure of said storage tank by operation of a venting means and opening said storage valve to admit said catalyst to a predetermined level in said addition hopper, said addition hopper communicating through an addition valve to a carrier gas line leading to said converter; c. closing said venting means and pressurizing said addition hopper to a second addition pressure; d. thereafter opening said addition valve and permitting said addition hopper to empty into said carrier gas line; e. after emptying of said addition hopper, closing said addition valve, opening said venting means to reduce the pressure in said addition hopper to said first pressure, and opening said storage valve to admit additional catalyst to fill said addition hopper to a predetermined level determined by the volume of said addition hopper; f. thereafter closing said venting means, closing said storage valve and admitting additional gases to raise the pressure of said addition hopper to said addition pressure; g. thereafter opening said addition valve to admit additional catalyst to said carrier gas line and repeating the above cycle.",
    "2. A process according to claim 1 wherein the duration of opening of each of said valves is controlled by timing means.",
    "3. A process according to claim 2 wherein the position of each of said valves is controlled by a sequencing control center.",
    "4. A process according to claim 1 wherein said addition valve is closed substantially whenever said storage valve is open and wherein said storage valve is closed substantially whenever said addition valve is open, and wherein said venting means is open whenever said storage valve is open and wherein said storage valve is closed whenever said venting means is closed.",
    "5. A process according to claim 4 wherein said venting means communicates with an upper portion of said catalyst storage tank.",
    "6. A process according to claim 1 wherein said storage tank has a first pressure of approximately atmospheric pressure."
  ],
  "cpc": [
    "B01J 8/0015",
    "B01J 2208/00752",
    "B01J 8/0035",
    "C10G 11/18",
    "C10G 11/187"
  ],
  "assignees": [
    "MARATHON OIL CO"
  ],
  "filing_date": "1975-01-14",
  "publication_date": "1977-04-19",
  "grant_date": "1977-04-19",
  "priority_date": "1975-01-14",
  "application_number": "US-54371975-A",
  "family_id": "24169297",
  "citations": [
    "US1535991A",
    "US2786800A",
    "US2892773A",
    "US3090593A",
    "US3156537A",
    "US3479093A",
    "US3850582A"
  ]
}

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