Michael J. Veraa
Engineering at Soaring Frst Dr, Houston, TX

License number
Louisiana PE.0019572
Issued Date
Jul 28, 1981
Category
Civil Engineer
Type
Chemical Engineer
Address
Address
16915 Soaring Forest Dr, Houston, TX 77059

Professional information

Michael Veraa Photo 1

Low Temperature Steam Stripping For Byproduct Polymer And Solvent Recovery From An Ethylene Oligomerization Process

US Patent:
8524972, Sep 3, 2013
Filed:
Apr 18, 2012
Appl. No.:
13/449839
Inventors:
Michael W. Weber - Houston TX, US
Randy L. Foster - Crosby TX, US
James R. Lattner - Laporte TX, US
Jimmy L. Tardy - Crosby TX, US
Michael J. Veraa - Houston TX, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
International Classification:
C07C 7/00, B01D 3/38
US Classification:
585809, 585802, 208255, 208356, 208362
Abstract:
This disclosure relates generally to low temperature steam stripping methods for byproduct polymer and solvent separation from an ethylene oligomerization process. The methods disclosed have been found to separate byproduct polymer from solvent without fouling process equipment or causing other process problems. The byproduct polymer ends up as flowable solid particles in a water stream that may be easily discharged from the process, while solvent is recovered for recycle to the process. In embodiments of the invention, over 90 wt % of the solvent used is recovered and the discharged byproduct polymer is less than 20 wt % solvent.


Michael Veraa Photo 2

Separation Of Olefin Vapor From Liquid Fraction To Reduce Fouling

US Patent:
2008018, Aug 7, 2008
Filed:
Feb 2, 2007
Appl. No.:
11/701790
Inventors:
Cor F. Van Egmond - Pasadena TX, US
Michael J. Veraa - Houston TX, US
Steven E. Silverberg - Seabrook TX, US
Michael P. Nicoletti - Houston TX, US
John Richard Shutt - Merchtem, BE
International Classification:
B01D 11/00
US Classification:
210634
Abstract:
This invention is directed to methods of removing water and other condensable materials, as well as solids particles such as catalyst particles, from olefin product streams so as to reduce fouling in the liquid and vapor separation equipment. In order to reduce fouling or contamination in the condensing or quenching process, this invention includes adding a hydrocarbon to at least a portion of the condensed liquid fraction in an amount that effects separation of the liquid fraction into upper and lower fractions.


Michael Veraa Photo 3

Alcohol And Olefin Production From Syngas

US Patent:
2008003, Feb 7, 2008
Filed:
Jun 20, 2007
Appl. No.:
11/820754
Inventors:
James R. Lattner - LaPorte TX, US
Matthew James Vincent - Baytown TX, US
Kun Wang - Bridgewater NJ, US
Michel Molinier - Houston TX, US
Michael J. Veraa - Houston TX, US
Anthony F. Volpe - Santa Clara CA, US
Hailian Li - Fremont CA, US
Jeffrey C. Yoder - San Jose CA, US
Mark Muraoka - Mountain View CA, US
International Classification:
C07C 29/00, B01J 21/04, B01J 23/02
US Classification:
568897, 502340, 502342, 502344, 502346, 568895
Abstract:
This invention is directed to a process for making alcohol from syngas, and a process for making olefin, as well as polyolefin, from the alcohol. The syngas is converted to a mixed alcohol stream using a catalyst comprising at least one oxide component. Upon contacting the catalyst with a desired syngas composition, a preferred mixed alcohol product is formed. Preferably, the syngas composition has a stoichiometric molar ratio of less than 2.


Michael Veraa Photo 4

Converting Methanol And Ethanol To Light Olefins

US Patent:
2006014, Jul 6, 2006
Filed:
Mar 8, 2005
Appl. No.:
11/075286
Inventors:
Philip Ruziska - Kingwood TX, US
Christopher Jenkins - Houston TX, US
James Lattner - Seabrook TX, US
Michael Nicoletti - Houston TX, US
Michael Veraa - Houston TX, US
Cor van Egmond - Pasadena TX, US
International Classification:
C07C 1/00
US Classification:
585639000
Abstract:
The present invention provides processes for producing light olefins from a feedstock comprising methanol and ethanol. The ethanol is converted to ethylene and water over a dehydration catalyst, while the methanol is converted to light olefins and water over a molecular sieve catalyst. These conversion steps may occur in two separate reactors operating in series or in parallel, or in a single reactor containing a mixture of dehydration catalyst and molecular sieve catalyst.


Michael Veraa Photo 5

Production Of Light Olefins

US Patent:
8415518, Apr 9, 2013
Filed:
Jun 14, 2007
Appl. No.:
11/818333
Inventors:
Richard B. Hall - Whitehouse Station NJ, US
Guang Cao - Branchburg NJ, US
Christopher David William Jenkins - South Caulfield, AU
James R. Lattner - LaPorte TX, US
Michael J. Veraa - Houston TX, US
Thomas H. Colle - Houston TX, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
International Classification:
C07C 1/20
US Classification:
585640, 585329, 585501, 585638, 585639
Abstract:
This invention is directed to a process for producing olefin product from an oxygenate feed that includes dimethyl ether (DME). The process uses an olefin forming catalyst that contains a porous crystalline material, preferably a porous crystalline aluminosilicate molecular sieve material. The process produces high quantities of light olefin (i. e. , ethylene, propylene, and mixtures thereof).


Michael Veraa Photo 6

Synthesis Gas Production And Use

US Patent:
7772292, Aug 10, 2010
Filed:
Apr 13, 2007
Appl. No.:
11/786922
Inventors:
Christopher David William Jenkins - South Caulfield, AU
James R. Lattner - La Porte TX, US
Michael J. Veraa - Houston TX, US
Keith H. Kuechler - Friendswood TX, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
International Classification:
C07C 27/00, C07C 1/00
US Classification:
518702, 518700, 518703, 518704
Abstract:
A method of producing synthesis gas for methanol synthesis that comprises the steps of: (a) obtaining a hydrogen stream that has greater than 5 mol % methane from an external process; (b) feeding into a reforming reactor: (i) a feed gas that comprises methane, (ii) water in a specified amount, (iii) oxygen in a specified amount, and (iv) the hydrogen stream in a specified amount; (c) reacting the feed gas, water, oxygen and the hydrogen stream in the reactor; and (d) withdrawing from the reactor the synthesis gas that is at a specific temperature, has less than 3 mol % methane, and has a stoichiometric number of from 1. 9 to 2. 3.