Reducing surface and bulk contamination in plastic

1. A method to extract contaminates from a first plastic to produce a purer plastic comprising:

a. providing a first plastic comprising individual contaminants, each individual contaminant having a concentration;

b. extracting said individual contaminates from said first plastic at a temperature and a pressure, using a leaching solvent that is at least one of THF, di-ethyl ether, hexanes, acetone, ethanol, methanol, propanol, iso-propanol, MEK, methylene chloride, or Ethyl Acetate, in extraction stages, wherein the total extraction time is less than about 6 hours, to produce a purer plastic comprising individual contaminates, each having a concentration;

wherein said extraction is flooded leaching wherein said temperature is between about 20 and 90 C; wherein said extraction stages are conducted at a leaching solvent to first plastic mass ratio; wherein said a leaching solvent to first plastic mass ratio per stage is greater than about 5:1 but less than 100:1; wherein said pressure is between about atmospheric and 1,000 atm; wherein said first plastic individual contaminants comprise at least one of 4-tertpentylphenol, bisphenol A, OCDD, PCB 118, and 2-ethylhexyl phthalate; wherein each individual contaminants concentration in said purer plastic is reduced compared to each individual contaminants concentration in said first plastic; and wherein the average of said reductions of said concentrations of said first plastic contaminants to said purer plastic contaminants is at least about 55% or LOQ; and

wherein the leaching solvent should not significantly dissolve the first plastic at the temperature and pressure of the process.

2. The method of claim 1 , wherein said number of stages is between about 1 and about 50.

3. The method of claim 1 , wherein said first plastic is a reclaimed plastic comprising at least one of a post-industrial or post-consumer film.

4. The method of claim 1 , wherein said first plastic has a mass average surface area to volume ratio of at least about 1 mm-1.

5. The method of claim 1 , wherein said first plastic is surface washed in a non-densified state by a surface washing process or processes prior to extraction and wherein said surface washing process or processes results in a greater than about an 80% reduction in loosely bound surface contamination; wherein said first plastic prior to surface washing has a surface area to volume ratio of greater than about 1 mm-1.

6. The method of claim 5 , wherein said surface washing process is of the de-inking type; wherein said de-inking process results in a delta E percent change of less than about 10% between the de-inked first plastic and the first plastic without surface printed ink.

7. The method of claim 1 , wherein said period of time represented by the sum of times for the individual flooded leaching stages is less than about 360 minutes.

8. The method of claim 1 , wherein said leaching solvent is purified after said flooded leaching or said flooded leaching stage or stages to allow re-use in the flooded leaching process by a solvent purification process or processes; wherein said solvent purification process or processes comprises at least one stage of distillation, physical adsorption or absorption of the chemical contaminants from the contaminated leaching solvent.

9. The method of claim 1 , wherein said first plastic is a reclaimed plastic that is at least one of a post-industrial or post-consumer film; wherein said post-consumer film includes post-commercial film and/or post-household film.

10. The method of claim 1 ; wherein said flooded leaching is a continuous stirred tank; wherein said first plastic is surface washed in a non-densified state by a surface washing process or processes prior to extraction and wherein said surface washing process or processes results in a greater than about an 80% reduction in loosely bound surface contamination; wherein said first plastic prior to surface washing has a surface area to volume ratio of greater than about 1 mm-1; wherein said surface washing process is of the de-inking type; wherein said de-inking process results in a delta E percent change of less than about 10% between the de-inked first plastic and the first plastic without surface printed ink; wherein said leaching solvent is ethyl acetate; wherein said continuous stirred tank involves 3 stages; wherein said temperature is about 77 C and near atmospheric pressure; wherein said ethyl acetate to first plastic ratio is about 20:1 per stage and for a residence time of about 20 minutes per stage; wherein the first plastic is de-volatilized and densified using melt extrusion to produce a purified pellet; wherein the purification process results in an average removal efficiency for 4-tertpentylphenol, bisphenol A, OCDD, PCB 118, and 2-ethylhexyl phthalate of greater than about 55%.

11. The method of claim 1 , wherein the leaching solvent comprises at least one of methane, ethane, propane, normal butane, isobutane, normal pentane, isopentane, neopentane, hexanes, heptanes, or octanes.