RECYCLE CONTENT GLYCOL ETHER AND GLYCOL ETHER ESTER COMPOSITIONS

1 .- 2 . (canceled)

3 . A method of making a recycle content glycol ether composition (“r-GE”), said method comprising reacting a recycle content alkylene oxide composition at least a portion of which is derived directly or indirectly from pyrolyzing a recycled waste (“pr-AO”) with hydrogen to produce a glycol ether effluent comprising r-GE.

4 .- 6 . (canceled)

7 . A method of making glycol ether, said method comprising:

a. a glycol ether manufacturer obtaining an alkylene oxide composition from a supplier and either:

i. from said supplier, also obtaining a pyrolysis recycle content allotment or

ii. from any person or entity, obtaining a pyrolysis recycle content allotment without a supply of an alkylene oxide composition from said person or entity transferring said pyrolysis recycle content allotment; and

b. said glycol ether manufacturer making a glycol ether composition (“GE”) from any alkylene oxide composition obtained from any source; and

c. either:

i. applying said pyrolysis recycle content allotment to GE made by the supply of alkylene oxide obtained in step (a); or

ii. applying said pyrolysis recycle content allotment to GE not made by the supply of alkylene oxide obtained in step (a), or

iii. depositing said pyrolysis recycle content allotment into a recycle inventory from which is deducted a recycle content value and applying at least a portion of said value to:

1. GE to thereby obtain r-GE, or

2. to a compound or composition other than GE, or

3. both;

whether or not the recycle content value is obtained from a pyrolysis recycle content allotment obtained in step a(i) or step a(ii).

8 . (canceled)

9 . A method of making a recycle content glycol ether composition (“r-GE”), said method comprising:

a. reacting any alkylene oxide composition in a synthetic process to make a glycol ether composition (“GE”); and

b. applying a recycle content value to at least a portion of said GE to thereby obtain a recycle content glycol ether composition (“r-GE”); and

c. optionally, obtaining said recycle content value by deducting at least a portion of said recycle content value from a recycle inventory, further optionally said recycle inventory also containing a pyrolysis recycle content allotment or a pyrolysis recycle content allotment deposit having been made into the recycle inventory prior to the deduction; and

d. optionally communicating to a third party that said r-GE has recycle content or is obtained or derived from recycled waste.

113 - 12 . (canceled)

13 . The method according to claim 9 , said method further comprising:

a. pyrolyzing a pyrolysis feed comprising a recycled waste material to thereby form a pyrolysis effluent comprising recycle pyoil (r-pyoil) and/or a recycle pygas (“r-pygas”);

b. optionally cracking a cracker feed comprising at least a portion of the r-pyoil to thereby produce a cracker effluent comprising r-olefins; or optionally cracking a cracker feed without r-pyoil to make olefins and applying a recycle content value to the olefins so made by deducting a recycle content value from a recycle inventory and applying it to the olefins to make r-olefins; and

c. reacting any olefin volume in a synthetic process to make a alkylene oxide composition; and

d. reacting at least a portion of any alkylene oxide composition in a synthetic process to make a glycol ether composition; and

e. applying a recycle content value to at least a portion of said glycol ether composition based on:

i. feeding a pyrolysis recycle content alkylene oxide composition (“pr-AO”) as a feedstock or

ii. depositing at least a portion of an allotment obtained from any one or more of steps a) or b) into a recycle inventory and deducting from said inventory a recycle content value and applying at least a portion of said value to GE to thereby obtain said r-GE.

14 .- 29 . (canceled)

30 . A recycle content glycol ether ester (“r-GEE”) having a reaction product derived from a recycle content glycol ether composition (“r-GE”) obtained by the method according to claim 9 .

31 . A recycle content glycol ether composition (“r-GE”) obtained by the method according to claim 9 .

32 . The method according to claim 9 , wherein said recycle content value is derived directly or indirectly from cracking r-pyoil or obtained from r-pygas.

33 . The method according to claim 9 , wherein said r-olefin, r-AO, or r-GE, or r-GEE is derived directly or indirectly from cracking r-pyoil in a gas fed cracker furnace.

34 . The method according to claim 9 , wherein the GE composition is prepared by reacting, in the presence of a catalyst, r-AO with alcohol.

35 . The method according to claim 9 , wherein at least a portion of the alkylene oxide composition is derived directly or indirectly from the pyrolysis of recycled waste and/or through the cracking of r-pyoil to thereby obtain an r-AO composition.

36 .- 39 . (canceled)

40 . The method according to claim 9 , wherein the glycol ether is made by a glycol ether manufacturer and the recycle content is apportioned among products made by a glycol ether manufacturer or the products made by any one entity or a combinations of entities among the Family of Entities of which the glycol ether manufacturer is a part, and wherein the method for apportioning is an asymmetric distribution of recycle content values among their product(s), and optionally at least one of the products is glycol ether and/or glycol ether ester.

41 . (canceled)

42 . The method according to claim 9 , wherein the glycol ether is made by a glycol ether manufacturer and the recycle content is apportioned among products made by a glycol ether manufacturer or the products made by any one entity or a combinations of entities among the Family of Entities of which the glycol ether manufacturer is a part, and wherein the method for apportioning is applied symmetrically or asymmetrically across a combination of GE and other products.

43 . The method according to claim 9 , wherein the AO is supplied by an AO supplier that transfers a recycle content allotment to the GE manufacturer and a supply of AO to the GE manufacturer.

44 . The method according to claim 9 , wherein the recycle content allotment is not associated with the AO supplied or the GE supplied.

45 .- 47 . (canceled)

48 . The method according to claim 9 , wherein the AO supplied is r-AO and at least a portion of the recycle content allotment being transferred is the recycle content in the r-AO supplied.

49 .- 52 . (canceled)

53 . The method according to claim 9 , wherein the recycle content value applied to GE is drawn from a recycle inventory that is derived directly or indirectly from the pyrolysis of recycled waste.

54 . (canceled)

55 . The method according to claim 9 , wherein an GE manufacturer or a person or entity among its Family of Entities obtains a supply of AO and an allotment, and at least a portion of the allotment is either:

a. applied to GE made from the AO supplied;

b. applied to GE not made by the supply of AO; or

c. deposited into a recycle inventory from which is deducted a recycle content value and applying at least a portion of the recycle content value to:

i. GE to thereby obtain r-GE, or

ii. to a compound or composition other than GE, or

iii. both; or

d. deposited into a recycle inventory and stored.

56 .- 66 . (canceled)

67 . The method according to claim 9 , wherein:

a. an olefin supplier either:

i. cracks a cracker feedstock comprising recycle pyoil to make an olefin composition at least a portion of which is obtained by cracking said recycle pyoil (r-olefin), or

ii. makes a pygas at least a portion of which is obtained by pyrolyzing a recycled waste stream (r-pygas), or

iii. both; and

b. a glycol ether manufacturer:

i. obtaining an allotment derived directly or indirectly with said r-olefin or said r-pygas from the supplier or a third-party transferring said allotment,

ii. making glycol ether from alkylene oxide, and

iii. associating at least a portion of the allotment with at least a portion of the glycol ether, whether or not the alkylene oxide used to make the glycol ether contains r-alkylene oxide.

68 . The method according to claim 9 , comprising:

a. making a r-olefin by either cracking the r-pyoil or separating an olefin from the r-pygas; and

b. converting at least a portion of the r-olefin in a synthetic process to make alkylene oxide, and

c. converting at least a portion of any or said alkylene oxide to glycol ether; and

d. applying a recycle content value to said glycol ether to make a r-GE; and

e. optionally, also making a r-pyoil or r-pygas or both by pyrolyzing a recycle feedstock.

69 .- 70 . (canceled)

71 . The method according to claim 9 , comprising:

a. glycol ether (“GE”), and

b. an identifier associated with said GE, said identifier being a representation that said GE has recycle content or is made from a source having recycle content.

72 .- 73 . (canceled)