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David Luis Woracek

from Yelm, WA
Age ~77

David Woracek Phones & Addresses

  • 8610 Rathbun Rd, Yelm, WA 98597 (360) 400-5117
  • Edgewood, WA
  • 29002 19Th St, Federal Way, WA 98003 (253) 946-0439
  • Seatac, WA
  • Thornton, WA

Work

Company: Kennedy/jenks consultants Position: Semi retired

Education

Degree: Master of Business Administration, Masters School / High School: University of Puget Sound 1978 to 1980

Industries

Civil Engineering

Professional Records

License Records

David Woracek

Address:
32001 32 Ave S #100, Federal Way, WA
License #:
44990 - Expired
Category:
Professional
Issued Date:
Aug 15, 2006
Expiration Date:
Sep 30, 2015

Resumes

Resumes

David Woracek Photo 1

David Woracek

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Location:
P/O Box 1251, Yelm, WA
Industry:
Civil Engineering
Work:
Kennedy/Jenks Consultants
Semi Retired
Education:
University of Puget Sound 1978 - 1980
Master of Business Administration, Masters

Business Records

Name / Title
Company / Classification
Phones & Addresses
David Woracek
Professional Engineer
JMS Construction
Engineering Services
32001 32 Ave S STE 100, Auburn, WA 98001
(253) 838-2230

Publications

Us Patents

So.sub.3 Flue Gas Conditioning System

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US Patent:
47792078, Oct 18, 1988
Filed:
Jan 6, 1987
Appl. No.:
7/000582
Inventors:
David L. Woracek - Federal Way WA
Robert A. Wright - Poway WA
Assignee:
The Chemithon Corporation - Seattle WA
International Classification:
G06F 1546
B03C 366
US Classification:
364500
Abstract:
An air pollution control system for injecting a conditioning agent into the flue gas of a power generator. The conditioning agent changes the resistivity of particulate matter in the flue gas, rendering the particulate matter more easily able to accept an electrostatic charge. Control of the conditioning gas injection rate is monitored by periodically sampling the average input power supplied to the power supplies of the electrostatic flue gas conditioning system. A proportional-integral controller receives the signal representing the difference between the average input power and a predetermined threshold signal. The control signal produced by the proportional integral controller causes incremental changes in the rate at which the conditioning agent, such as SO. sub. 3, is added to the flue gas.

Flue Gas Conditioning System

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US Patent:
52883035, Feb 22, 1994
Filed:
Apr 7, 1992
Appl. No.:
7/864847
Inventors:
David L. Woracek - Federal Way WA
Robert A. Wright - Indianapolis IN
Assignee:
Wilhelm Environmental Technologies, Inc. - Indianapolis IN
International Classification:
B03C 301
B03C 368
US Classification:
95 2
Abstract:
A flue gas conditioning system features a self-contained sulfur burner control loop that operates to maintain a constant desired temperature supply of sulfur dioxide in air by varying the rate of supply of sulfur fuel to the sulfur burner, and the absence of device in the sulfur flow path to measure or monitor sulfur flow rate. In the system, a conditioning agent demand signal operates either a means to supply the sulfur burner with a flow of air, or an air heater in the air flow path upstream of the sulfur burner, or both, to provide conditions that would increase or decrease the temperature of the sulfur burner output absent the self-contained sulfur burner control loop, and as a result of the operation of the self-contained sulfur burner control loop, systems of the invention can provide a demanded flow of sulfur dioxide and air at a substantially constant concentration and a desired temperature to a catalytic converter in response to a conditioning agent demand signal.

Sulfur Dioxide Generation Using Granulated Or Emulsoid Sulfur Feedstock

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US Patent:
60457708, Apr 4, 2000
Filed:
Jun 3, 1997
Appl. No.:
8/204208
Inventors:
Kent S. Duncan - late of St. Louis MO
David L. Woracek - Federal Way WA
Michael J. Lentz - Indianapolis IN
Assignee:
Wilhelm Environmental Technologies - Indianapolis IN
International Classification:
C01B 1754
US Classification:
423543
Abstract:
A flue gas conditioning system (FGC) for conditioning the flue gas flowing in a flue from a boiler to an electrostatic precipitator by injecting sulfur trioxide into the flue gas upstream of the electrostatic precipitator. The FGC has a source (52) of granulated sulfur which is transported by a conveyor (54) to a sulfur furnace (60) where it is combusted in sulfur dioxide. The sulfur dioxide flows from the sulfur furnace (60) into a catalytic converter 62 which generates sulfur trioxide therefrom. The sulfur trioxide flows from the catalytic converter 62 into probes 64 which are mounted in the flue duct. Alternatively, the FGC has a source (70) of emulsoid sulfur which is pumped by a sulfur pump (72) to the inlet of an atomizing spray nozzle (200) which atomizes the emulsoid sulfur and sprays it into sulfur furnace (50).
David Luis Woracek from Yelm, WA, age ~77 Get Report