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Roy H Whipp

from Saint Petersburg, FL
Age ~76

Roy Whipp Phones & Addresses

  • 400 Beach Dr NE UNIT 1501, St Petersburg, FL 33701 (352) 324-3152
  • Saint Petersburg, FL
  • 8343 Lakeshore Blvd, Yalaha, FL 34797 (352) 324-3152
  • 116 Butler St, Windermere, FL 32806 (407) 876-6973
  • Clermont, FL
  • Miami, FL
  • 400 Beach Dr NE UNIT 1501, Saint Petersburg, FL 33701

Resumes

Resumes

Roy Whipp Photo 1

President At Whipp Technology

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Position:
President at Whipp technology, President at Whipp Technology
Location:
Tampa/St. Petersburg, Florida Area
Industry:
Mining & Metals
Work:
Whipp technology since Jun 1976
President

Whipp Technology since Jun 1976
President
Roy Whipp Photo 2

Independent Computer Software Professional

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Location:
Tampa/St. Petersburg, Florida Area
Industry:
Computer Software
Roy Whipp Photo 3

Roy Whipp

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Business Records

Name / Title
Company / Classification
Phones & Addresses
Roy Whipp
Director
Whipp Technology Inc
Business Services
116 Butler St, Windermere, FL 34786
Roy H. Whipp
Director
Whipp Hart Enterprises, Inc
34 E Plant St, Winter Garden, FL 34787

Publications

Us Patents

Process And Plant For The Direct Reduction Of Particulate Iron-Oxide-Containing Material

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US Patent:
20020117024, Aug 29, 2002
Filed:
Jan 15, 2002
Appl. No.:
10/045061
Inventors:
Siegfried Zeller - Leonding, AT
Konstantin Millionis - St. Georgen, AT
Johann Reidetschlager - Linz, AT
Leopold Kepplinger - Leonding, AT
Johann Zirngast - Marchtrenk, AT
Johannes Schenk - Linz, AT
Roy Whipp - Windermere FL, US
Assignee:
Voest-Alpine Industrieanlagenbau GmbH
International Classification:
C21B013/14
US Classification:
075/450000, 266/172000
Abstract:
In a process for the direct reduction of particulate iron-oxide-containing material by fluidization, a synthesis as is introduced as a reducing gas into several fluidized bed zones consecutively arranged in series for the reducing gas and the reducing as is conducted from one fluidized bed zone to another fluidized bed zone in counterflow to the particulate iron-oxide containing material. In order to reduce operating costs and, in particular, the energy demand, a temperature of the iron-oxide-containing material of either below 400 C. and, preferably, below 350 C., or above 580 C. and, preferably about 650 C., or a temperature ranging from 400 C. to 580 C. is adjusted, in the first fluidized bed zone, wherein, at a temperature adjustment to below 400 C., the temperature range between 400 C. and 580 C. in the fluidized bed zone following the first fluidized bed zone in the flow direction of the iron-oxide-containing material is sassed through within a period of 10 minutes and, preferably within 5 minutes. and wherein, at a temperature adjustment to above 580 C., the temperature range between 400 C. and 580 C. is passed through within a period of time of maximally 10 minutes and, preferably, 5 minutes, and wherein. Furthermore, at a temperature adjustment in the range of from 400 C. to 580 C., the iron-oxide-containing material remains within that temperature range for a maximum of 10 minutes and. preferably, 5 minutes and is passed on into the fluidized bed zone following next immediately after having reached the desired temperature (FIG. ).

Process For Producing Sponge Iron By Direct Reduction Of Iron-Oxide-Containing Material

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US Patent:
61430536, Nov 7, 2000
Filed:
Sep 30, 1998
Appl. No.:
9/101292
Inventors:
Johann Reidetschlager - Linz, AT
Siegfried Zeller - Leonding, AT
Felix Wallner - Linz, AT
Roy Hubert Whipp - Windermere FL
Assignee:
Voest-Alpine Industrieanlagenbau GmbH - Linz
International Classification:
C21B 1300
US Classification:
75444
Abstract:
In a process for producing sponge iron by direct reduction of iron-oxide-containing material, synthesis gas is mixed with top gas forming in the direct reduction of the iron-oxide-containing material and is utilized as a CO- and H. sub. 2 -containing reducing gas for direct reduction and for heating the iron-oxide-containing material to a reduction temperature. To be able to save energy in an economically efficient manner when producing steel, especially in the refining process, direct reduction is carried out as follows: (1) in addition to the reducing gas, a carbon-containing gas, such as natural gas, or a gas having higher hydrocarbons is utilized for reduction; (2) the iron-oxide-containing material for a predetermined period of time exceeding the period necessary for complete reduction is exposed to the reducing gas and to the additionally supplied carbon-containing gas, and (3) a CO/CO. sub. 2 ratio ranging between 2 and 5, preferably a ratio in excess of 2. 5, is adjusted in the reducing gas.

Method And Arrangement For Cooling Hot Bulk Material

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US Patent:
60483814, Apr 11, 2000
Filed:
Oct 15, 1997
Appl. No.:
8/875303
Inventors:
Leopold Werner Kepplinger - Leonding, AT
Gerhard Cip - Linz, AT
Anton Himmel - Alberndorf, AT
Karl-Heinz Zimmerbauer - Hargelsberg, AT
Roland Sachsenhofer - Linz, AT
Roy Hubert Whipp - Windermere FL
Assignee:
Voest-Alpine Industrieanlagenbau GmbH - Linz
Brifer International Ltd. - Bridgetown
International Classification:
C21B 1300
US Classification:
75436
Abstract:
In order to attain as low a final temperature as possible after as short a period of time as possible in a method of cooling hot briquetted sponge iron (3) under optimum utilization of the cooling medium, the hot briquetted sponge iron (3), in a first cooling step (11), is passed exclusively by a gaseous cooling medium while being gently cooled and subsequently, in a second cooling step (14), is sprayed with a liquid cooling medium, thus being intensively cooled to the final temperature desired.

Process And Plant For Avoiding Metal Dusting In The Direct Reduction Of Iron-Oxide-Containing Materials

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US Patent:
58580581, Jan 12, 1999
Filed:
Jan 15, 1997
Appl. No.:
8/765331
Inventors:
Gerald Kern - Vienna, AT
Werner Leopold Kepplinger - Leonding, AT
Johannes Schenk - Linz, AT
Roy Hubert Whipp - Windermere FL
Assignee:
Voest-Alpine Industrieanlagenbau GmbH
Brifer International Ltd.
International Classification:
C21B 1300
US Classification:
75505
Abstract:
A direct reduction process is disclosed for iron-oxide-containing materials. Synthesis gas is mixed with top gas produced during direct reduction of the iron-oxide-containing materials and is used as reduction gas for directly reducing iron-oxide-containing materials. In order to avoid or reduce metal dusting caused by an increased CO content of the reduction gas with a simple technique and equipment, the CO/CO. sub. 2 ratio of the reduction gas is set at a predetermined value from 1 to 3.

Direct Reduction Process For Iron Oxide-Containing Materials

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US Patent:
58556435, Jan 5, 1999
Filed:
Jan 15, 1997
Appl. No.:
8/765339
Inventors:
Gerhard Cip - Linz, AT
Konstantin Milionis - St. Georgen an der Stiefling, AT
Sadat Morteza Guscheh - Linz, AT
Roy Hubert Whipp - Windermere FL
Assignee:
Voest-Alpine Industrieanlagenbau GmbH - Linz
International Classification:
C21B 1300
US Classification:
75380
Abstract:
In a process for the direct reduction of iron-oxide containing material, synthesis gas is mixed with top gas formed in the direct reduction of the iron-oxide containing material and is used as a reducing gas for direct reduction. In order to avoid metal dusting despite an elevated CO-content of the reducing gas, or to reduce metal dusting, in a procedurally simple and cost-saving manner while minimizing the energy demand, an H. sub. 2 O content of between 1 and 2%, preferably amounting to about 1. 5%, is achieved in the reducing gas by subjecting a partial volume of the top gas to CO. sub. 2 scrubbing prior to being used as a reducing gas, wherein the top gas subjected to CO. sub. 2 scrubbing is mixed with the synthesis gas, is brought to a predetermined temperature by direct water irrigation while being saturated with H. sub. 2 O, after direct water irrigation is heated to a temperature above the saturation temperature by admixing CO. sub. 2 -unscrubbed top gas, and subsequently is used as a reducing gas.

Process For The Direct Reduction Of Particulate Iron-Containing Material And A Plant For Carrying Out The Process

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US Patent:
58337342, Nov 10, 1998
Filed:
Jul 24, 1997
Appl. No.:
8/849838
Inventors:
Gerhard Cip - Linz, AT
Gottfried Rossmann - Linz, AT
Konstantin Milionis - St. Georgen, AT
Roy Hubert Whipp - Windermere FL
Assignee:
Voest-Alpine Industrieanlagenbau GmbH
Brifer International Ltd.
International Classification:
C22B 514
US Classification:
75450
Abstract:
With a process for the direct reduction of particulate iron-containing material by fluidization, reformed gas, at least partially freed from CO. sub. 2, is supplied to a fluidized-bed reduction zone as a reducing gas and is carried off from the same as a top gas and at least a portion of the top gas together with reformed gas is utilized for direction reduction. To economize on parts of the plant that are impinged on by reducing gas and in order to achieve savings in terms of heating costs, CH. sub. 4 and N. sub. 2 are, in addition to CO. sub. 2, at least partially removed by adsorption, from 50 to 100% of the reformed as and 0 to 100% of the top gas, and the tail gas removed from the reformed gas and/or the top gas by adsorption is utilized as a heating gas.
Roy H Whipp from Saint Petersburg, FL, age ~76 Get Report