Hybrid sustainable composites and methods of making and using thereof
US-2016229997-A1 · Aug 11, 2016 · US
US2017107334A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017107334-A1 |
| Application number | US-201515126187-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 13, 2015 |
| Priority date | Mar 14, 2014 |
| Publication date | Apr 20, 2017 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Biocarbon is presented as an alternative to synthetic carbon black. Master batches having biocarbon for usage in raw plastics and/or the production of composites. Biocarbon is mainly derived from plant biomass, but other sources can be used. A method of producing the master batch: (a) pyrolyzing processed biomass in an oxygen-starved environment to produced biocarbon; (b) comminuting the biocarbon in a reduced oxygen atmosphere; (c) cooling the comminuted biocarbon; (d) mixing the cooled comminuted biocarbon with a carrier resin, thereby producing the master batch.
Opening claim text (preview).
1 . A master batch for the production of composites, the master batch comprising a blend of elemental carbon and a carrier resin, wherein the elemental carbon is derived from pyrolized biomass. 2 . The master batch of claim 1 , wherein the master batch comprises from about 25% wt. to about 75% wt. of elemental carbon and from about 25% wt. to about 75% wt. of the carrier resin. 3 . (canceled) 4 . The master batch of claim 1 , wherein the biomass is selected from: plant fibers, municipal solid waste, agricultural biomass, forest biomass, and animal manure. 5 . The master batch of claim 1 , wherein the carrier resin is a synthetic polymer. 6 . The master batch of claim 4 , wherein the synthetic polymer is selected from polyethylene (PE), crosslinked-polyethylene (PEX), polypropylene (PP), impact polypropylene, and polybutylene (PB); polyvinylchloride (PVC), chlorinated polyvinyl chloride (CPVC), polyvinylidene fluoride (PVDF), polystyrene (PS), acrylic polymers, nylon, acrylonitrile butadiene styrene, thermoplastic polyurethanes, polycarbonates, or combinations thereof. 7 . The master batch of claim 1 , wherein the carrier resin is a bioplastic. 8 . The master batch of claim 7 , wherein the bioplastic is selected from poly(lactic acid) (PLA), polyglycolic acid (PGA), poly(lactic acid-co-glycolic acid (PLGA), polycaprolactone, polyhydroxyalkanoates or combinations thereof. 9 . The master batch of claim 1 , wherein the blend further comprises an additive. 10 - 11 . (canceled) 12 . A composite comprising a polymer compounded with a master batch of claim 1 . 13 . The composite of claim 12 , wherein the composite comprises between 1% wt. and 6% wt. of the elemental carbon. 14 . A product comprising the composite of claim 12 . 15 . A method of producing a master batch, the method comprising: (a) pyrolyzing processed biomass in an oxygen-starved environment to produced biocarbon; (b) comminuting the biocarbon; (c) mixing the comminuted biocarbon with a carrier resin, thereby producing the master batch. 16 . The method of claim 15 , wherein the pyrolysis is carried out at a temperature of about 400° C. to about 900° C. 17 . The method of claim 16 , wherein the biocarbon is comminuted while the biocarbon is at about 350° C. 18 . The method of claim 15 , wherein the comminuting of step (b) takes place in a reduced oxygen atmosphere. 19 . The method of claim 18 , wherein the method further comprises cooling the comminuted biocarbon. 20 . The method of claim 19 , wherein the comminuted biocarbon is cooled to about 200° C. 21 . The method of claim 15 , wherein the biocarbon is comminuted to a particle size ranging from about 100 microns to about 50 nanometers. 22 . The method of claim 15 , wherein from about 25% wt. to about 70% wt of the carrier resin is mixed with from about 30% wt. to about 75% wt. of the biocarbon. 23 . The method of claim 15 , wherein the method further comprises adding an additive.
Masterbatches · CPC title
using a polymer as a carrier · CPC title
Waste processing or separation · CPC title
Polypropene · CPC title
Compositions of unspecified macromolecular compounds · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.