Clifton S Goddin

Deceased

from Tulsa, OK

Also known as:
  • Clifton Sylvanus Goddin
  • Clifton S Godding
  • Clifton S Gooddin
Phone and address:
3303 100Th St, Tulsa, OK 74137
9182980730

Clifton Goddin Phones & Addresses

  • 3303 100Th St, Tulsa, OK 74137 • 9182980730 • 9187431883 • 9189952141
  • 3303 100Th Pl, Tulsa, OK 74137 • 9182980730 • 9187431883
  • 3903 Riverside Dr #16, Tulsa, OK 74105 • 9182980730
  • 201 E 41St St S #4, Tulsa, OK 74105 • 9182980730
  • 3845 S 103Rd East Ave STE 100, Tulsa, OK 74146 • 9186050570

Work

  • Position:
    Administrative Support Occupations, Including Clerical Occupations

Education

  • Degree:
    High school graduate or higher

Us Patents

  • Process For Producing Sweet Co.sub.2 And Hydrocarbon Streams

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  • US Patent:
    45579113, Dec 10, 1985
  • Filed:
    Jun 28, 1984
  • Appl. No.:
    6/625490
  • Inventors:
    Clifton S. Goddin - Tulsa OK
    Boyd E. Cabanaw - Tulsa OK
  • Assignee:
    Amoco Corporation - Chicago IL
  • International Classification:
    C01B 1716
    C01B 3120
  • US Classification:
    423228
  • Abstract:
    In a preferred embodiment, carbon dioxide and hydrogen sulfide are removed from a gaseous stream also containing a recoverable hydrocarbon product by CO. sub. 2 sweetening, bulk CO. sub. 2 removal, and hydrocarbon sweetening absorption steps, each absorption utilizing the same alkanolamine as absorbent. According to another aspect, each amine can be selected from the group consisting of tertiary amines and sterically hindered amines. According to yet another aspect, a feed gas comprising hydrogen sulfide and carbon dioxide can be introduced successively into a carbon dioxide sweetening absorption zone, then into a bulk CO. sub. 2 removal absorption zone, then into a hydrocarbon sweetening absorption zone. Alternatively, a feed gas comprising hydrogen sulfide and carbon dioxide can be introduced first into a bulk CO. sub. 2 removal absorption zone and then streams from the bulk CO. sub.
  • Cryogenic Distillative Removal Of Co.sub.2 From High Co.sub.2 Content Hydrocarbon Containing Streams

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  • US Patent:
    44591420, Jul 10, 1984
  • Filed:
    Oct 1, 1982
  • Appl. No.:
    6/432217
  • Inventors:
    Clifton S. Goddin - Tulsa OK
  • Assignee:
    Standard Oil Company (Indiana) - Chicago IL
  • International Classification:
    F25J 302
  • US Classification:
    62 17
  • Abstract:
    Carbon dioxide is removed from a carbon dioxide containing hydrocarbon stream having a varying composition of light lean oil components in the C. sub. 3 through C. sub. 10 range. A light lean oil recycle stream of predetermined carbon number range is produced and utilized in the cryogenic distillative process.
  • Co.sub.2 Removal From High Co.sub.2 Content Hydrocarbon Containing Streams

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  • US Patent:
    45294119, Jul 16, 1985
  • Filed:
    Apr 30, 1984
  • Appl. No.:
    6/605716
  • Inventors:
    Clifton S. Goddin - Tulsa OK
    Edward A. Turek - Tulsa OK
    Boyd A. George - Lisle IL
  • Assignee:
    Standard Oil Company - Chicago IL
  • International Classification:
    B01D 5322
  • US Classification:
    55 16
  • Abstract:
    Carbon dioxide is removed from CO. sub. 2 and hydrocarbon containing gaseous streams. In the instance where the hydrocarbons and CO. sub. 2 are such that hydrocarbons would condense out during CO. sub. 2 removal, the gas stream is treated in one or more stages to accomplish hydrocarbon composition control.
  • Method For Removal Of Sulfur Deposited On A Claus Catalyst

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  • US Patent:
    41805542, Dec 25, 1979
  • Filed:
    Aug 14, 1978
  • Appl. No.:
    5/933370
  • Inventors:
    Clifton S. Goddin - Tulsa OK
    John W. Palm - Tulsa OK
  • Assignee:
    Standard Oil Company (Indiana) - Chicago IL
  • International Classification:
    C01B 1704
  • US Classification:
    423574R
  • Abstract:
    An improved method of regenerating a low temperature Claus catalyst bed having elemental sulfur deposited on the catalyst involving initially using a moderately hot effluent gas (typically 600. degree. to 650. degree. F. ) from the first conventional Claus reactor to warm up the low temperature Claus reactor and remove deposited sulfur and after the outlet temperature of said low temperature reactor reaches a value high enough to decompose COS and CS. sub. 2 (typically 600. degree. to 650. degree. F. ), supplementing the moderately hot first conventional Claus reactor effluent gas with hot (typically 1000. degree. to 1200. degree. F. ) waste heat boiler effluent such that the temperature of the regenerating catalyst bed can be elevated to about 700. degree. F. or higher. The intentional temperature excursion to about 700. degree. F.
  • Co.sub.2 Removal From High Co.sub.2 Content Hydrocarbon Containing Streams

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  • US Patent:
    44669461, Aug 21, 1984
  • Filed:
    Mar 12, 1982
  • Appl. No.:
    6/357362
  • Inventors:
    Clifton S. Goddin - Tulsa OK
    Edward A. Turek - Tulsa OK
    Boyd A. George - Lisle IL
  • Assignee:
    Standard Oil Company (Indiana) - Chicago IL
  • International Classification:
    B01D 5334
  • US Classification:
    423228
  • Abstract:
    Carbon dioxide is removed from CO. sub. 2 and hydrocarbon containing gaseous streams. In the instance where the hydrocarbons and CO. sub. 2 are such that hydrocarbons would condense out during CO. sub. 2 removal, the gas stream is treated in one or more stages to accomplish hydrocarbon composition control.
  • Low Temperature Claus Process With Water Removal

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  • US Patent:
    44303173, Feb 7, 1984
  • Filed:
    Jan 28, 1982
  • Appl. No.:
    6/343661
  • Inventors:
    Robert L. Reed - Tulsa OK
    Luther E. Petty - Darien IL
    Clifton S. Goddin - Tulsa OK
  • Assignee:
    Standard Oil Company (Indiana) - Chicago IL
  • International Classification:
    C01B 1704
    B01J 804
  • US Classification:
    423574R
  • Abstract:
    Claus process sulfur recovery can be improved by performing a Claus conversion under low temperature and low water concentration conditions. The process treats a feed stream containing sulfur compounds by conversion of all sulfur components to hydrogen sulfide, water removal to low water concentrations, creation of a Claus reaction mixture, and then low temperature catalytic conversion to sulfur and water.

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