National Renewable Energy Laboratory 1978 - 2012
Research Fellow
Skills:
Sustainability Energy Policy Energy Efficiency Research Science Biofuels Solar Energy Energy Climate Change Chemistry Biomass Environmental Awareness Environmental Policy Characterization Renewable Energy Nanotechnology Sustainable Development
Helena L. Chum - Arvada CO Giuseppe Filardo - Palermo, IT
Assignee:
Midwest Research Institute - Kansas City MO
International Classification:
B01D 1100
US Classification:
210634
Abstract:
A process is disclosed for separating low molecular weight components from complex aqueous organic mixtures. The process includes preparing a separation solution of supercritical carbon dioxide with an effective amount of an entrainer to modify the solvation power of the supercritical carbon dioxide and extract preselected low molecular weight components. The separation solution is maintained at a temperature of at least about 70. degree. C. and a pressure of at least about 1,500 psi. The separation solution is then contacted with the organic mixtures while maintaining the temperature and pressure as above until the mixtures and solution reach equilibrium to extract the preselected low molecular weight components from the organic mixtures. Finally, the entrainer/extracted components portion of the equilibrium mixture is isolated from the separation solution.
Controlled Catalytic And Thermal Sequential Pyrolysis And Hydrolysis Of Phenolic Resin Containing Waste Streams To Sequentially Recover Monomers And Chemicals
Helena L. Chum - Arvada CO Robert J. Evans - Lakewood CO
Assignee:
MRI Ventures, Inc. - Kansas City MO
International Classification:
C07C 3700 C07C 3752
US Classification:
568806
Abstract:
A process of using fast pyrolysis in a carrier gas to convert a waste phenolic resin containing feedstreams in a manner such that pyrolysis of said resins and a given high value monomeric constituent occurs prior to pyrolyses of the resins in other monomeric components therein comprising: selecting a first temperature program range to cause pyrolysis of said resin and a given high value monomeric constituent prior to a temperature range that causes pyrolysis of other monomeric components; selecting, if desired, a catalyst and a support and treating said feedstreams with said catalyst to effect acid or basic catalyzed reaction pathways to maximize yield or enhance separation of said high value monomeric constituent in said first temperature program range to utilize reactive gases such as oxygen and steam in the pyrolysis process to drive the production of specific products; differentially heating said feedstreams at a heat rate within the first temperature program range to provide differential pyrolysis for selective recovery of optimum quantity of said high value monomeric constituent prior to pyrolysis of other monomeric components therein; separating said high value monomeric constituent; selecting a second higher temperature program range to cause pyrolysis of a different high value monomeric constituent of said phenolic resins waste and differentially heating said feedstreams at said higher temperature program range to cause pyrolysis of said different high value monomeric constituent; and separating said different high value monomeric constituent.
Controlled Catalytic And Thermal Sequential Pyrolysis And Hydrolysis Of Polymer Waste Comprising Nylon 6 And A Polyolefin Or Mixtures Of Polyolefins To Sequentially Recover Monomers Or Other High Value Products
Robert J. Evans - Lakewood CO Helena L. Chum - Arvada CO
Assignee:
Midwest Research Institute - Kansas City MO
International Classification:
C07D20112 C07C 400
US Classification:
540540
Abstract:
A process of using fast pyrolysis in a carrier gas to convert a plastic waste feedstream having a mixed polymeric composition in a manner such that pyrolysis of a given polymer to its high value monomeric constituent occurs prior to pyrolysis of other plastic components therein comprising: selecting a first temperature program range to cause pyrolysis of said given polymer to its high value monomeric constituent prior to a temperature range that causes pyrolysis of other plastic components; selecting a catalyst and support for treating said feed streams with said catalyst to effect acid or base catalyzed reaction pathways to maximize yield or enhance separation of said high value monomeric constituent in said temperature program range; differentially heating said feed stream at a heat rate within the first temperature program range to provide differential pyrolysis for selective recovery of optimum quantities of the high value monomeric constituent prior to pyrolysis of other plastic components; separating the high value monomeric constituents; selecting a second higher temperature range to cause pyrolysis of a different high value monomeric constituent of said plastic waste and differentially heating the feedstream at the higher temperature program range to cause pyrolysis of the different high value monomeric constituent; and separating the different high value monomeric constituent.
Sequential Pyrolysis Of Plastic To Recover Polystyrene Hcl And Terephthalic Acid
Robert J. Evans - Lakewood CO Helena L. Chum - Arvada CO
Assignee:
Midwest Research Institute - Kansas City MO
International Classification:
F23G 712
US Classification:
423488
Abstract:
A process of pyrolyzing plastic waste feed streams containing polyvinyl chloride, polyethylene terephthalate, polystyrene and polyethylene to recover polystyrene HCl and terephthalic acid comprising: heating the plastic waste feed stream to a first temperature; adding an acid or base catalyst on an oxide or carbonate support; heating the plastic waste feed stream to pyrolyze polyethylene terephthalate and polyvinyl chloride; separating terephthalic acid or HCl; heating to a second temperature to pyrolyze polystyrene; separating styrene; heating the waste feed stream to a third temperature to pyrolyze polyethylene; and separating hydrocarbons.
Process For Preparing Phenolic Formaldehyde Resole Resin Products Derived From Fractionated Fast-Pyrolysis Oils
Helena L. Chum - Arvada CO Roland E. Kreibich - Auburn WA
Assignee:
Midwest Research Institute - Kansas City MO
International Classification:
C08G 804 C08J 8906 B32B 2108
US Classification:
528129
Abstract:
A process for preparing phenol-formaldehyde resole resins and adhesive compositions in which portions of the phenol normally contained in said resins are replaced by a phenol/neutral fractions extract obtained from fractionating fast-pyrolysis oils.
Controlled Catalytic And Thermal Sequential Pyrolysis And Hydrolysis Of Mixed Polymer Waste Streams To Sequentially Recover Monomers Or Other High Value Products
Robert J. Evans - Lakewood CO Helena L. Chum - Arvada CO
Assignee:
Midwest Research Institute - Kansas City MO
International Classification:
C07D30708
US Classification:
549429
Abstract:
A process of using fast pyrolysis in a carrier gas to convert a plastic waste feedstream having a mixed polymeric composition in a manner such that pyrolysis of a given polymer to its high value monomeric constituent occurs prior to pyrolysis of other plastic components therein comprising: selecting a first temperature program range to cause pyrolysis of said given polymer to its high value monomeric constituent prior to a temperature range that causes pyrolysis of other plastic components; selecting a catalyst and support for treating said feed streams with said catalyst to effect acid or base catalyzed reaction pathways to maximize yield or enhance separation of said high value monomeric constituent in said temperature program range; differentially heating said feed stream at a heat rate within the first temperature program range to provide differential pyrolysis for selective recovery of optimum quantities of the high value monomeric constituent prior to pyrolysis of other plastic components; separating the high value monomeric constituents; selecting a second higher temperature range to cause pyrolysis of a different high value monomeric constituent of said plastic waste and differentially heating the feedstream at the higher temperature program range to cause pyrolysis of the different high value monomeric constituent; and separating the different high value monomeric constituent.
Controlled Catalystic And Thermal Sequential Pyrolysis And Hydrolysis Of Polycarbonate And Plastic Waste To Recover Monomers
Robert J. Evans - Lakewood CO Helena L. Chum - Arvada CO
Assignee:
Midwest Research Institute - Kansas City MO
International Classification:
C07C 100 C07C 400
US Classification:
585241
Abstract:
A process of using fast pyrolysis to convert a plastic waste feed stream containing polycarbonate and ABS to high value monomeric constituents prior to pyrolysis of other plastic components therein comprising: selecting a first temperature program range to cause pyrolysis of a given polymer to its high value monomeric constituents prior to a temperature range that causes pyrolysis of other plastic components; selecting an acid or base catalysts and an oxide or carbonate support for treating the feed stream to affect acid or base catalyzed reaction pathways to maximize yield or enhance separation of the high value monomeric constituents of polycarbonate and ABS in the first temperature program range; differentially heating the feed stream at a heat rate within the first temperature program range to provide differential pyrolysis for selective recovery of optimum quantities of the high value monomeric constituents prior to pyrolysis or other plastic components; separating the high value monomeric constituents from the polycarbonate to cause pyrolysis to a different high value monomeric constituent of the plastic waste and differentially heating the feed stream at the second higher temperature program range to cause pyrolysis of different high value monomeric constituents; and separating the different high value monomeric constituents.
Phenolic Compounds Containing/Neutral Fractions Extract And Products Derived Therefrom From Fractionated Fast-Pyrolysis Oils
Helena L. Chum - Arvada CO Stuart K. Black - Denver CO James P. Diebold - Lakewood CO Roland E. Kreibich - Auburn WA
Assignee:
Midwest Research Institute Ventures, Inc. - Kansas City MO
International Classification:
C07C 3720 C08G 1402
US Classification:
528129
Abstract:
A process for preparing phenol-formaldehyde novolak resins and molding compositions in which portions of the phenol normally contained in said resins are replaced by a phenol/neutral fractions extract obtained from fractionating fast-pyrolysis oils. The fractionation consists of a neutralization stage which can be carried out with aqueous solutions of bases or appropriate bases in the dry state, followed by solvent extraction with an organic solvent having at least a moderate solubility parameter and good hydrogen bonding capacity. Phenolic compounds-containing/neutral fractions extracts obtained by fractionating fast-pyrolysis oils from a lignocellulosic material, is such that the oil is initially in the pH range of 2-4, being neutralized with an aqueous bicarbonate base, and extracted into a solvent having a solubility parameter of approximately 8. 4-9. 11 [cal/cm. sup. 3 ]. sup. 1/2 with polar components in the 1. 8-3.