throbber
William(cid:3)C.(cid:3)Jones(cid:3)
`
`213(cid:3)N.(cid:3)Beacon(cid:3)Shores(cid:3)Dr.(cid:3)(cid:3)
`(cid:3)Seneca,(cid:3)SC(cid:3)(cid:3)29672(cid:3)(cid:3)(cid:3)(cid:3)(cid:3)(cid:3)(cid:3)(cid:3)
`
`(cid:3)(cid:3)Home:(cid:3)(cid:3)(cid:3)864(cid:882)882(cid:882)3025(cid:3)(cid:3)(cid:3)(cid:3)(cid:3)Cell:(cid:3)(cid:3)864(cid:882)508(cid:882)4516(cid:3)
`(cid:3)lakeinsc@bellsouth.net(cid:3)
`
`Education:(cid:3)
`B.S.(cid:3)Chemical(cid:3)Engineering,(cid:3)Virginia(cid:3)Tech(cid:3)
`1965(cid:3)(cid:882)(cid:3)1969(cid:3)
`1969(cid:3)(cid:882)(cid:3)1970(cid:3) M.S.(cid:3)Chemical(cid:3)Engineering,(cid:3)Virginia(cid:3)Tech(cid:3)
`1975(cid:3)(cid:882)(cid:3)1978(cid:3) M.S.(cid:3)Engineering(cid:3)Administration,(cid:3)University(cid:3)of(cid:3)Tennessee(cid:3)
`
`1978(cid:3)–(cid:3)1980(cid:3)
`1980(cid:3)–(cid:3)1982(cid:3)
`
`1992(cid:3)–(cid:3)1993(cid:3)
`
`1993(cid:3)–(cid:3)1999(cid:3)
`1994(cid:3)–(cid:3)1999(cid:3)
`
`Work(cid:3)Experience:(cid:3)
`1970(cid:3)–(cid:3)1971(cid:3)
`Ashland(cid:3)Oil(cid:3)Inc.,(cid:3)Ashland,(cid:3)KY,(cid:3)Process(cid:3)Engineer(cid:3)for(cid:3)Refinery(cid:3)Operations(cid:3)
`1971(cid:3)–(cid:3)1973(cid:3)
`U.(cid:3)S.(cid:3)Army,(cid:3)Picatinny(cid:3)Arsenal,(cid:3)NJ,(cid:3)Lieutenant,(cid:3)Ordnance(cid:3)Corps,(cid:3)Munitions(cid:3)R&D(cid:3)
`Eastman(cid:3)Chemical(cid:3)Company:(cid:3)
`1974(cid:3)–(cid:3)2003(cid:3)
`1974(cid:3)–(cid:3)1978(cid:3)
`Process(cid:3)Improvement(cid:3)Engineer(cid:3)supporting(cid:3)manufacture(cid:3)of(cid:3)various(cid:3)(cid:3)
`chemicals(cid:3)such(cid:3)as(cid:3)Acetaldehyde,(cid:3)Acetic(cid:3)Acid,(cid:3)Acetic(cid:3)Anhydride,(cid:3)Acetate(cid:3)
`Esters,(cid:3)Ketones,(cid:3)TPA(cid:3)and(cid:3)DMT(cid:3)
`Pilot(cid:3)Plant(cid:3)Engineer(cid:3)responsible(cid:3)for(cid:3)Chemicals(cid:3)(cid:3)(Acids(cid:3)and(cid:3)Anhydrides)(cid:3)pilot(cid:3)plant(cid:3)
`(cid:3)
`Pilot(cid:3)Plant(cid:3)Group(cid:3)Supervisor(cid:3)responsible(cid:3)for(cid:3)piloting(cid:3)Methyl(cid:3)Acetate,(cid:3)(cid:3)
`Acetic(cid:3)Acid,(cid:3)Catalyst(cid:3)Recovery(cid:3)and(cid:3)other(cid:3)chemicals(cid:3)
`1982(cid:3)–(cid:3)1984(cid:3) Manufacturing(cid:3)Staff(cid:3)Engineer/Operations(cid:3)Manager(cid:3)for(cid:3)Acetic(cid:3)Anhydride(cid:3)(via(cid:3)Ketene)(cid:3)
`1984(cid:3)–(cid:3)1985(cid:3)
`Supervisor(cid:3)of(cid:3)Process(cid:3)Improvement(cid:3)Engineering(cid:3)Group(cid:3)(cid:3)
`1985(cid:3)–(cid:3)1987(cid:3)
`Acetic(cid:3)Anhydride(cid:3)(via(cid:3)Carbonylation)(cid:3)Manufacturing(cid:3)Staff(cid:3)and(cid:3)Operations(cid:3)(cid:3)
`Manager(cid:3)for(cid:3)the(cid:3)Methanol,(cid:3)Methyl(cid:3)Acetate,(cid:3)and(cid:3)Catalyst(cid:3)Recovery(cid:3)Section(cid:3)
`1987(cid:3)–(cid:3)1988(cid:3) Operations(cid:3)Manager(cid:3)for(cid:3)Chemical(cid:3)Manufacturing(cid:3)of(cid:3)Plasticizers,(cid:3)Acetate(cid:3)(cid:3)
`Esters,(cid:3)Triacetin,(cid:3)Crotonic(cid:3)Acid,(cid:3)2(cid:882)Ethyl(cid:3)Hexanoic(cid:3)Acid(cid:3)
`1988(cid:3)–(cid:3)1992(cid:3) Operations(cid:3)Manager(cid:3)for(cid:3)Design,(cid:3)Construction,(cid:3)Commissioning,(cid:3)and(cid:3)(cid:3)
`Start(cid:882)up(cid:3)of(cid:3)Eastman’s(cid:3)second(cid:3)Acetic(cid:3)Anhydride(cid:3)Plant(cid:3)via(cid:3)Carbonylation.(cid:3)
`Project(cid:3)Team(cid:3)Manager(cid:3)of(cid:3)Innovations(cid:3)Team(cid:3)for(cid:3)development(cid:3)of(cid:3)Nickel(cid:3)Catalyzed(cid:3)Acetic(cid:3)(cid:3)
`Acid(cid:3)Process(cid:3)from(cid:3)methanol(cid:3)and(cid:3)carbon(cid:3)monoxide.(cid:3)
`R&D(cid:3)Manager(cid:3)for(cid:3)Process(cid:3)Improvement(cid:3)and(cid:3)Pilot(cid:3)Plant(cid:3)Supervisors,(cid:3)Acid(cid:3)Division(cid:3)(cid:3)
`Eastman's(cid:3)Program(cid:3)Manager(cid:3)for(cid:3)Department(cid:3)of(cid:3)Energy(cid:3)(Clean(cid:3)Coal)(cid:3)funded(cid:3)Commercial(cid:3)(cid:3)
`Demonstration(cid:3)of(cid:3)Liquid(cid:3)Phase(cid:3)Methanol(cid:3)Process(cid:3)with(cid:3)Air(cid:3)Products,(cid:3)Inc.(cid:3)(cid:3)Worked(cid:3)with(cid:3)(cid:3)
`DOE(cid:3)and(cid:3)Air(cid:3)Products(cid:3)Program(cid:3)Managers(cid:3)to(cid:3)oversee(cid:3)the(cid:3)Project(cid:3)construction,(cid:3)start(cid:882)up(cid:3)(cid:3)
`and(cid:3)operation(cid:3)during(cid:3)the(cid:3)four(cid:882)year(cid:3)project(cid:3)demonstration.(cid:3)
`Director(cid:3)of(cid:3)Technology(cid:3)for(cid:3)Eastman’s(cid:3)Licensing(cid:3)Group(cid:3)responsible(cid:3)for(cid:3)Technical(cid:3)support(cid:3)(cid:3)
`and(cid:3)project(cid:3)development(cid:3)of(cid:3)various(cid:3)Licensing(cid:3)Projects(cid:3)including(cid:3)acetic(cid:3)acid,(cid:3)coal(cid:3)(cid:3)
`gasification,(cid:3)terephthalic(cid:3)acid(cid:3)and(cid:3)other(cid:3)projects.(cid:3)(cid:3)
`2003(cid:3)–(cid:3)2007(cid:3)(cid:3)(cid:3)(cid:3)(cid:3) Retired(cid:3)from(cid:3)Eastman(cid:3)Chemical(cid:3)in(cid:3)2003(cid:3)but(cid:3)continued(cid:3)as(cid:3)part(cid:882)time(cid:3)consultant(cid:3)to(cid:3)(cid:3)
`Eastman(cid:3)on(cid:3)several(cid:3)International(cid:3)Licensing(cid:3)Projects(cid:3)involving(cid:3)acetic(cid:3)acid(cid:3)and(cid:3)derivatives.(cid:3)(cid:3)
`Consultant(cid:3)to(cid:3)Saudi(cid:3)International(cid:3)Petrochemical(cid:3)Co,(cid:3)(Sipchem),(cid:3)on(cid:3)(cid:3)
`design,(cid:3) construction,(cid:3)commissioning(cid:3)and(cid:3)startup(cid:3)of(cid:3)an(cid:3)(cid:3)Acetic(cid:3)Acid(cid:3)Plant(cid:3)in(cid:3)Saudi(cid:3)(cid:3)
`Arabia.(cid:3)(cid:3)Served(cid:3)as(cid:3)Commissioning(cid:3)and(cid:3)Startup(cid:3)Manager(cid:3)for(cid:3)Acetic(cid:3)Acid(cid:3)Plant(cid:3)startup,(cid:3)(cid:3)
`NOV(cid:3)2009(cid:3)(cid:882)(cid:3)FEB(cid:3)2010:(cid:3)(cid:3)Lead(cid:3)a(cid:3)100+(cid:3)member(cid:3)multi(cid:882)cultural(cid:3)team(cid:3)of(cid:3)operators(cid:3)and(cid:3)(cid:3)
`engineers(cid:3)for(cid:3)Plant(cid:3)Commissioning(cid:3)and(cid:3)Start(cid:882)up.(cid:3)(cid:3)2011(cid:882)(cid:3)PRESENT:(cid:3)(cid:3)Continued(cid:3)consulting(cid:3)(cid:3)
`on(cid:3)(cid:3)debottlenecking(cid:3)and(cid:3)process(cid:3)improvement(cid:3)for(cid:3)the(cid:3)Acetyls(cid:3)Plant(cid:3)and(cid:3)for(cid:3)Ethyl(cid:3)(cid:3)
`Acetate(cid:3)Plant.(cid:3)
`
`1999(cid:3)–(cid:3)2003(cid:3)
`
`2008(cid:3)–(cid:3)2015(cid:3)
`
`000001
`
`(cid:44)(cid:51)(cid:53)(cid:3)(cid:49)(cid:82)(cid:17)(cid:3)(cid:21)(cid:19)(cid:20)(cid:24)(cid:16)(cid:19)(cid:19)(cid:20)(cid:26)(cid:20)
`(cid:40)(cid:91)(cid:75)(cid:76)(cid:69)(cid:76)(cid:87)(cid:3)(cid:20)(cid:19)(cid:22)(cid:27)
`
`

`
`Patents:(cid:3)
`
`US Patent No. 5,922,911
`Title: Process for the manufacture of acetic anhydride
`Inventors: William Crawford Jones, Eleanor Hawkins Cwirko
`Original Assignee: Eastman Chemical CompanyFiling date: Apr 24, 1998
`Issue date: Jul 13, 1999(cid:3)
`Abstract: Disclosed is a carbonylation process for the manufacture of acetic anhydride wherein the
`utilization of carbon monoxide is increased. The process involves the liquid phase manufacture of
`acetic anhydride by contacting a mixture of (i) a reactant compound selected from methyl acetate,
`dimethyl ether or a mixture thereof, (ii) methyl iodide, (iii) catalyst components comprising
`rhodium and one or more promoters, and (iv) dissolved carbon monoxide in a carbonylation zone
`in which carbon monoxide is not fed below the surface of the mixture in a manner to increase the
`concentration of carbon monoxide in the liquid reaction mixture.
`
`International Application No.:PCT/US2011/059699
`No.:
`WO/2012/064689
`International Filing Date:
`Publication Date: 18.05.2012
`08.11.2011
`Applicants: EASTMAN CHEMICAL COMPANY [US/US]; 200 South Wilcox Drive
`Kingsport, TN 37660 (US)
`Inventors: LANE, Donald, Wayne; (US).
`CONAWAY, Randall, Lee; (US).
`PARTIN, Lee, Reynolds; (US).
`BEWLEY, Jerry, Lee; (US).
`JONES, William, Crawford; (US).
`BAYS, Joseph, Nathaniel; (US)
`MCGREEVEY, William, K.; P.O. Box 511 Kingsport, TN 37662-5075 (US)
`
`Agent:
`Priority
`Data:
`Title
`
`Abstract:
`
`61/413,212 12.11.2010 US
`
`PROCESSING GASEOUS STREAMS RESULTING FROM
`CARBONYLATION PROCESS
`(EN)The invention provides methods for recovering iodine-containing compounds from a
`gaseous stream that contain at least one iodine-containing compound. The method includes:
`(a) contacting the gaseous stream with liquid methyl acetate in a first scrubbing zone to
`produce a methyl acetate- scrubbed gaseous stream and a first used scrubbant, the first
`used scrubbant containing methyl acetate, acetic acid, and the iodide compound; and (b)
`contacting at least some of the methyl acetate-scrubbed gaseous stream with liquid acetic
`acid in a second scrubbing zone to produce an acetic acid- scrubbed gaseous stream and a
`second used scrubbant, the second used scrubbant containing methyl acetate and acetic
`acid. The method may further include a third scrubber step that includes contacting at least
`some of the acetic acid-scrubbed gaseous stream with water in a third scrubbing zone to
`produce a water-scrubbed gaseous stream and a third used scrubbant, the third used
`scrubbant containing water and acetic acid. The gaseous stream may also contain other
`components, for example hydrogen, carbon monoxide, methyl acetate, acetic acid, acetic
`anhydride, nitrogen, ethylidene diacetate, methane, argon or a combination of two or more of
`the foregoing. Optionally, at least some of the third used scrubbant with reactants may be
`combined in a chemical process that uses mixtures of acetic acid and water.
`
`000002

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