Gregory Lowman resumes & CV records
Resumes
Gregory M Lowman, Age 51327 Bowline Ct, Severna Park, MD 21146
Gregory Lowman Phones & Addresses
327 Bowline Ct, Severna Park, MD 21146 (410) 647-4960
Aurora, NC
Bolivia, NC
1775 Harbor Dr, Chester, MD 21619 (410) 695-1784 (410) 643-3815
Pasadena, MD
Brunswick, NC
Millersville, MD
Odenton, MD
Hull, GA
1775 Harbor Dr, Chester, MD 21619 (410) 770-0458
Social networks
Gregory M Lowman
Linkedin
Work
Position:
Sales Occupations
Education
Degree:
High school graduate or higher
Mentions for Gregory M Lowman
Publications & IP owners
Us Patents
Cooling Tower With Indirect Heat Exchanger
US Patent:
2017016, Jun 8, 2017
Filed:
Dec 3, 2015
Appl. No.:
14/958445
Inventors:
- Jessup MD, US
Zan Liu - Clarksville MD, US
Branislav Korenic - Columbia MD, US
John Edward Rule - Mooney Mooney, AU
Preston P. Blay - Silver Spring MD, US
Philip S. Hollander - Silver Spring MD, US
Glenn David Comisac - Catonsville MD, US
Gregory Michael Lowman - Chester MD, US
Zan Liu - Clarksville MD, US
Branislav Korenic - Columbia MD, US
John Edward Rule - Mooney Mooney, AU
Preston P. Blay - Silver Spring MD, US
Philip S. Hollander - Silver Spring MD, US
Glenn David Comisac - Catonsville MD, US
Gregory Michael Lowman - Chester MD, US
International Classification:
F28C 1/14
F28D 1/047
F28F 25/12
F28F 25/04
F28F 25/06
F28D 5/02
F28D 1/02
F28D 1/047
F28F 25/12
F28F 25/04
F28F 25/06
F28D 5/02
F28D 1/02
Abstract:
A heat exchange apparatus is provided with an indirect evaporative heat exchange section. The indirect evaporative heat exchange section includes a series of serpentine tubes, and an evaporative liquid is passed downwardly onto the indirect heat exchange section. The evaporative liquid is collected in a sump and then pumped upwardly to be distributed again across the indirect heat exchange section.An improved heat exchange apparatus is provided with an indirect evaporative heat exchange section including a series of serpentine tubes with run sections and return bend sections of both normal and increased height. A direct heat exchange section may be provided in the vertical spacing between run sections formed by the increased height return bends.
Cooling Tower With Indirect Heat Exchanger
US Patent:
2016013, May 19, 2016
Filed:
Jan 25, 2016
Appl. No.:
15/005652
Inventors:
- Jessup MD, US
Zan Liu - Clarksville MD, US
Branislav Korenic - Columbia MD, US
John Edward Rule - Mooney Mooney, AU
Preston P. Blay - Silver Spring MD, US
Philip S. Hollander - Silver Spring MD, US
Glenn David Comisac - Catonsville MD, US
Gregory Michael Lowman - Chester MD, US
Zan Liu - Clarksville MD, US
Branislav Korenic - Columbia MD, US
John Edward Rule - Mooney Mooney, AU
Preston P. Blay - Silver Spring MD, US
Philip S. Hollander - Silver Spring MD, US
Glenn David Comisac - Catonsville MD, US
Gregory Michael Lowman - Chester MD, US
International Classification:
F28C 1/14
Abstract:
A heat exchange apparatus is provided with an indirect evaporative heat exchange section. An evaporative liquid is passed downwardly onto the indirect heat exchange section. The evaporative liquid is collected in a sump and then pumped upwardly to be distributed again across the indirect heat exchange section.An improved heat exchange apparatus is provided with two indirect evaporative heat exchange sections separated by a vertical distance. A direct evaporative heat exchange section may be provided in the vertical spacing between the two indirect evaporative heat exchange sections.
Cooling Tower With Indirect Heat Exchanger
US Patent:
2014026, Sep 18, 2014
Filed:
Mar 15, 2013
Appl. No.:
13/833788
Inventors:
- Jessup MD, US
Zan Liu - Clarksville MD, US
Branislav Korenic - Columbia MD, US
John Edward Rule - Mooney Mooney, AU
Preston Blay - Silver Spring MD, US
Philip S. Hollander - Silver Spring MD, US
Glenn David Comisac - Catonsville MD, US
Gregory Michael Lowman - Chester MD, US
Zan Liu - Clarksville MD, US
Branislav Korenic - Columbia MD, US
John Edward Rule - Mooney Mooney, AU
Preston Blay - Silver Spring MD, US
Philip S. Hollander - Silver Spring MD, US
Glenn David Comisac - Catonsville MD, US
Gregory Michael Lowman - Chester MD, US
Assignee:
Baltimore Aircoil Company, Inc. - Jessup MD
International Classification:
F28D 5/02
US Classification:
261128
Abstract:
A heat exchange apparatus is provided with an indirect evaporative heat exchange section. The indirect evaporative heat exchange section is comprised of a series of serpentine tubes, and an evaporative liquid is passed downwardly onto the indirect heat exchange section. The evaporative liquid is collected in a sump and then pumped upwardly to be distributed again across the indirect heat exchange section. An improved heat exchange apparatus is provided with an indirect evaporative heat exchange section consisting of a series of serpentine tubes comprised of tube runs both of normal and increased height between tube runs A direct heat exchange section may be provided in the increased vertical spacing between tube runs A secondary spray distribution may also be provided in the increased vertical spacing between tube runs.
Cooling Tower With Indirect Heat Exchanger
US Patent:
2014026, Sep 18, 2014
Filed:
Mar 15, 2013
Appl. No.:
13/833971
Inventors:
- Jessup MD, US
Zan Liu - Clarksville MD, US
Branislav Korenic - Columbia MD, US
John Edward Rule - Mooney Mooney, AU
Preston Blay - Silver Spring MD, US
Philip S. Hollander - Silver Spring MD, US
Glenn David Comisac - Catonsville MD, US
Gregory Michael Lowman - Chester MD, US
Zan Liu - Clarksville MD, US
Branislav Korenic - Columbia MD, US
John Edward Rule - Mooney Mooney, AU
Preston Blay - Silver Spring MD, US
Philip S. Hollander - Silver Spring MD, US
Glenn David Comisac - Catonsville MD, US
Gregory Michael Lowman - Chester MD, US
Assignee:
Baltimore Aircoil Company, Inc. - Jessup MD
International Classification:
F28D 5/02
US Classification:
261128
Abstract:
A heat exchange apparatus is provided with an indirect evaporative heat exchange section. The indirect evaporative heat exchange section is comprised of a series of serpentine tubes, and an evaporative liquid is passed downwardly onto the indirect heat exchange section. The evaporative liquid is collected in a sump and then pumped upwardly to be distributed again across the indirect heat exchange section. An improved heat exchange apparatus is provided with an indirect evaporative heat exchange section consisting of a series of serpentine tubes comprised of run sections return bend sections of both normal and increased height. A direct heat exchange section may be provided in the vertical spacing between run sections formed by the increased height return bends.
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