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Charles L Hemler

from Mount Prospect, IL
Age ~82
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Also known as:
Chas L Hemler
Phone and address:
1141 Linneman Rd, Mount Prospect, IL 60056
(847) 427-1472
Related to:
Karen M Richelsen, 59Daniel J Hemler, 46Sherene L Hemler, 45Timothy J Hemler, 48Laura R Hemler, 57Aaron T Woosley, 56Christine A Weber, 73Kathleen A Hemler, 82
Connected to:
Brian M Hemler, 40Christopher J Hemler, 40Heidi A Hemler, 58James M Hemler, 77Kristi Hemler, 48Carol A Hemley, 95Jennifer L Hemlin, 40Scott J Hemlinger, 53Camille Hemlock, 64Mary A Hemlock, 69

Charles Hemler Phones & Addresses

  • 1141 Linneman Rd, Mount Prospect, IL 60056 (847) 427-1472
  • 607 N Windsor Dr, Mount Prospect, IL 60056 (847) 255-8261 (847) 873-0261
  • 1141 S Linneman Rd APT 1, Mt Prospect, IL 60056 (847) 255-8261
  • 607 N Windsor Dr, Mt Prospect, IL 60056 (847) 456-3488

Work

Position: Sales Occupations

Education

Degree: High school graduate or higher

Interests

job inquiries, expertise requests, busin...

Emails

c***[email protected]

Industries

Oil & Energy

Resumes

Resumes

Charles Hemler Photo 1

Technology Manager- Fcc At Uop

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Location:
Greater Chicago Area
Industry:
Oil & Energy
Experience:
UOP (Public Company; 1001-5000 employees; Oil & Energy industry): Technology Manager- FCC,  (-) 

Publications

Us Patents

Fcc Dual Elevation Riser Feed Distributors For Gasoline And Light Olefin Modes Of Operation

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US Patent:
20070205139, Sep 6, 2007
Filed:
Dec 29, 2006
Appl. No.:
11/617894
Inventors:
SATHIT KULPRATHIPANJA - Des Plaines IL, US
Daniel N. Myers - Des Plaines IL, US
Paolo Palmas - Des Plaines IL, US
Mark W. Schnaith - Des Plaines IL, US
Ismail B. Cetinkaya - Des Plaines IL, US
Peter J. Van Opdorp - Des Plaines IL, US
Charles L. Hemler - Des Plaines IL, US
International Classification:
C10G 11/00
US Classification:
208113
Abstract:
A fluid catalytic cracking process includes feeding hydrocarbon into a riser in the presence of a catalyst, cracking the hydrocarbon in the riser in the presence of the catalyst to form a cracked stream, and separating the catalyst from the cracked stream. When in a gasoline mode, the hydrocarbon is fed through a first distributor into the riser, and when in a light olefin mode, the hydrocarbon is fed through a second distributor into the riser. The second distributor is positioned at a higher elevation than the first distributor.

Fcc Reactor Arrangement For Sequential Disengagement And Progressive Temperature Reduction

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US Patent:
62482971, Jun 19, 2001
Filed:
Jan 6, 1995
Appl. No.:
8/369782
Inventors:
Laurence O. Stine - Western Springs IL
Charles L. Hemler - Mount Prospect IL
Carlos A. Cabrera - Northbrook IL
David A. Lomas - Barrington IL
Assignee:
UOP LLC - Des Plaines IL
International Classification:
F27B 1508
F27B 1504
US Classification:
422144
Abstract:
An FCC apparatus places a quench chamber above a reactor vessel and a hot stripper below a reactor vessel to provide a progressively decreasing temperature profile up the structure of the FCC arrangement and equipment for sequential reaction control. A riser contains the primary catalytic reactions of the hydrocarbon vapor and delivers the reacted vapors to the reactor structure. Starting from the bottom of the structure the hot stripper has the highest temperature and desorbs or displaces hydrocarbons from the catalyst to terminate long residence time catalytic reactions. Above the hot stripper bulk separation equipment divides the main vapor and catalyst stream to limit residence time of major catalytic reactions. At a yet higher elevation and lower internal temperature quench equipment arrests thermal reactions of the vapor stream. This structure arrangement permits reliable control of reaction time to obtain desired products and enhances mechanical reliability of the structure.

Fluidized Catalytic Cracking Process Utilizing A High Temperature Reactor

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US Patent:
52345785, Aug 10, 1993
Filed:
Sep 26, 1991
Appl. No.:
7/766498
Inventors:
Laurence O. Stine - Western Springs IL
Charles L. Hemler - Mount Prospect IL
Carlos A. Cabrera - Northbrook IL
David A. Lomas - Barrington IL
Assignee:
UOP - Des Plaines IL
International Classification:
C10G 1100
US Classification:
208113
Abstract:
The simultaneous use of lift gas in a riser zone that, operates above 975. degree. F. (525. degree. C. ) and directly transfers catalyst and hydrocarbons to a series of cyclone separators, the stripping of spent catalyst in a heated stripper zone for the recovery of additional hydrocarbon vapors, and the immediate quenching of a converted hydrocarbon feed upon leaving a cyclone separator raises the octane and product yield in an FCC process. The process uses the specific steps of passing regenerated catalyst particles into the lower section of a substantially vertical riser conversion zone at a temperature greater than 975. degree. F. and accelerating the particles up the riser by contact with a lift gas comprising C. sub. 3 and lighter hydrocarbons to a velocity of at least 1. 2 meters per second.
Control profile
Charles L Hemler from Mount Prospect, IL, age ~82 Get Report