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Malcolm Draper Phones & Addresses

  • 3075 E Kennedy Dr APT 301, Salt Lake Cty, UT 84108 (212) 595-9104
  • 3075 Kennedy Dr, Salt Lake Cty, UT 84108 (801) 582-0162 (801) 583-8971
  • Salt Lake City, UT
  • 310 72Nd St, New York, NY 10023 (212) 595-2930 (212) 595-9104
  • San Francisco, CA
  • Far Hills, NJ
  • Chatham, NJ
  • 310 W 72Nd St #14, New York, NY 10023

Work

Position: Executive, Administrative, and Managerial Occupations

Education

Degree: Associate degree or higher

Resumes

Resumes

Malcolm Draper Photo 1

Malcolm Draper

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Location:
New York, NY
Industry:
Financial Services
Malcolm Draper Photo 2

Malcolm Draper

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Publications

Us Patents

Aqueous Phase Oxidation Process

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US Patent:
7951988, May 31, 2011
Filed:
Apr 1, 2009
Appl. No.:
12/416412
Inventors:
George G. Foster - Salt Lake City UT, US
Frederick P. Kesler - Salt Lake City UT, US
Malcolm Draper - New York NY, US
Assignee:
Earth Renewal Group, LLC - Salt Lake City UT
International Classification:
A62D 3/11
US Classification:
588405, 210761
Abstract:
An improved oxidization process may be used to oxidize a wide variety of feedstocks. Oxidation takes place in a reactor where the feedstock is mixed with an oxidizing acid, such as nitric acid. The reaction mixture may also include a secondary oxidizing acid such as sulfuric acid as well as water and/or dissolved and mechanically mixed oxygen gas. The reactor may be maintained at an elevated pressure such as at least approximately 2070 kPa or desirably at least approximately 2800 kPa. The temperature of the reaction mixture may be maintained at no more than 210 C. In the various embodiments described herein, the process may include: combining recycled effluent from the reactor with the feedstock, combining one or more oxidizing acids with the feedstock, comminuting the feedstock to reduce the size of the particles, feeding the feedstock into the high pressure reactor at an approximately constant feed rate, dispersing oxygen gas from the headspace of the reactor into the reaction mixture, and/or removing all or almost all of the gas from the reactor through the liquid effluent.

Aqueous Phase Oxidation Process

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US Patent:
8115047, Feb 14, 2012
Filed:
Apr 1, 2009
Appl. No.:
12/416419
Inventors:
George G. Foster - Salt Lake City UT, US
Frederick P. Kesler - Salt Lake City UT, US
Malcolm Draper - New York NY, US
Assignee:
Earth Renewal Group, LLC - Salt Lake City UT
International Classification:
A62D 3/00
US Classification:
588405, 210908
Abstract:
An improved oxidization process may be used to oxidize a wide variety of feedstocks. Oxidation takes place in a reactor where the feedstock is mixed with an oxidizing acid, such as nitric acid. The reaction mixture may also include a secondary oxidizing acid such as sulfuric acid as well as water and/or dissolved and mechanically mixed oxygen gas. The reactor may be maintained at an elevated pressure such as at least approximately 2070 kPa or desirably at least approximately 2800 kPa. The temperature of the reaction mixture may be maintained at no more than 210 C. In the various embodiments described herein, the process may include: combining recycled effluent from the reactor with the feedstock, combining one or more oxidizing acids with the feedstock, comminuting the feedstock to reduce the size of the particles, feeding the feedstock into the high pressure reactor at an approximately constant feed rate, dispersing oxygen gas from the headspace of the reactor into the reaction mixture, and/or removing all or almost all of the gas from the reactor through the liquid effluent.

Aqueous Phase Oxidation Process

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US Patent:
8168847, May 1, 2012
Filed:
Apr 1, 2009
Appl. No.:
12/416438
Inventors:
George G. Foster - Salt Lake City UT, US
Frederick P. Kesler - Salt Lake City UT, US
Malcolm Draper - New York NY, US
Assignee:
Earth Renewal Group, LLC - Salt Lake City UT
International Classification:
A62D 3/38
US Classification:
588320, 588406
Abstract:
An improved oxidization process may be used to oxidize a wide variety of feedstocks. Oxidation takes place in a reactor where the feedstock is mixed with an oxidizing acid, such as nitric acid. The reaction mixture may also include a secondary oxidizing acid such as sulfuric acid as well as water and/or dissolved and mechanically mixed oxygen gas. The reactor may be maintained at an elevated pressure such as at least approximately 2070 kPa or desirably at least approximately 2800 kPa. The temperature of the reaction mixture may be maintained at no more than 210 C.

Aqueous Phase Oxidation Process

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US Patent:
8481800, Jul 9, 2013
Filed:
Apr 1, 2009
Appl. No.:
12/416431
Inventors:
George G. Foster - Salt Lake City UT, US
Frederick P. Kesler - Salt Lake City UT, US
Malcolm Draper - New York NY, US
Assignee:
Earth Renewal Group, LLC - Salt Lake City UT
International Classification:
A62D 3/30
US Classification:
588313, 588302
Abstract:
An improved oxidization process may be used to oxidize a wide variety of feedstocks. Oxidation takes place in a reactor where the feedstock is mixed with an oxidizing acid, such as nitric acid. The reaction mixture may also include a secondary oxidizing acid such as sulfuric acid as well as water and/or dissolved and mechanically mixed oxygen gas. The reactor may be maintained at an elevated pressure such as at least approximately 2070 kPa or desirably at least approximately 2800 kPa. The temperature of the reaction mixture may be maintained at no more than 210 C.

Aqueous Phase Oxidation Process

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US Patent:
20100254882, Oct 7, 2010
Filed:
Apr 1, 2009
Appl. No.:
12/416424
Inventors:
George G. Foster - Salt Lake City UT, US
Frederick P. Kesler - Salt Lake City UT, US
Malcolm Draper - New York NY, US
Assignee:
Earth Renewal Group, LLC - Salt Lake City UT
International Classification:
C01B 31/18
US Classification:
4234182
Abstract:
An improved oxidization process may be used to oxidize a wide variety of feedstocks. Oxidation takes place in a reactor where the feedstock is mixed with an oxidizing acid, such as nitric acid. The reaction mixture may also include a secondary oxidizing acid such as sulfuric acid as well as water and/or dissolved and mechanically mixed oxygen gas. The reactor may be maintained at an elevated pressure such as at least approximately 2070 kPa or desirably at least approximately 2800 kPa. The temperature of the reaction mixture may be maintained at no more than 210 C. In the various embodiments described herein, the process may include: combining recycled effluent from the reactor with the feedstock, combining one or more oxidizing acids with the feedstock, comminuting the feedstock to reduce the size of the particles, feeding the feedstock into the high pressure reactor at an approximately constant feed rate, dispersing oxygen gas from the headspace of the reactor into the reaction mixture, and/or removing all or almost all of the gas from the reactor through the liquid effluent.

Waste Treatment Process

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US Patent:
20120080383, Apr 5, 2012
Filed:
Sep 30, 2011
Appl. No.:
13/250308
Inventors:
Frederick P. Kesler - Salt Lake City UT, US
George G. Foster - Salt Lake City UT, US
Shannon Comp - New York NY, US
Malcolm Draper - New York NY, US
Assignee:
EARTH RENEWAL GROUP, LLC - Salt Lake City UT
International Classification:
C02F 1/72
C02F 1/62
C02F 1/68
C02F 1/52
C02F 1/42
US Classification:
210665, 210721, 210712
Abstract:
A process for treating waste includes reacting a feedstock in a reactor to form an effluent. The feedstock is part of a reaction mixture that includes sulfuric and nitric acid. The effluent is separated into a liquid fraction and a solid fraction. Heavy metals such as arsenic, cadmium, cobalt, mercury, molybdenum, and/or selenium are removed from the liquid fraction to form a cleaned liquid fraction. The reaction mixture, excluding solids, includes no more than 7.5 wt % of the total of the first oxidizing acid and the nitric acid.

Waste Treatment Process

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US Patent:
20130306575, Nov 21, 2013
Filed:
Jul 8, 2013
Appl. No.:
13/936932
Inventors:
Frederick P. Kesler - Salt Lake City UT, US
Malcolm Draper - New York NY, US
Shannon Comp - Cedar City UT, US
Assignee:
Earth Renewal Group, LLC - Salt Lake City UT
International Classification:
C02F 11/06
US Classification:
210758
Abstract:
A process for treating waste includes reacting an organic feedstock in a reactor. The organic feedstock is part of a reaction mixture that includes a first oxidizing acid (e.g., sulfuric acid) and nitric acid. The weight ratio of solids in the organic feedstock to the total of the first oxidizing acid and the nitric acid is at least 0.2. The weight ratio of solids in the organic feedstock to the first oxidizing acid is at least 0.3. The weight ratio of solids in the organic feedstock to the nitric acid is at least 0.5.

Waste Treatment Process

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US Patent:
20170203983, Jul 20, 2017
Filed:
Apr 3, 2017
Appl. No.:
15/478031
Inventors:
- Salt Lake City UT, US
Frederick P. Kesler - Salt Lake City UT, US
Malcolm Draper - New York City NY, US
Shannon L. Comp - Cedar City UT, US
Assignee:
Earth Renewal Group, LLC - Salt Lake City UT
International Classification:
C02F 1/72
C05B 17/02
C02F 11/06
Abstract:
An improved oxidation process may be used to oxidize a wide variety of feedstocks. Oxidation takes place in a reactor where the feedstock is mixed with an oxidizing acid, such as nitric acid. The reaction mixture may also include another oxidizing acid such as sulfuric acid.
Malcolm Tr Draper from Salt Lake City, UT, age ~72 Get Report