# US 10,870,739 B2 · Wax as a melt flow modifier and processing aid for polymers

> Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt

- Number: US 10,870,739 B2
- Document ID: US10870739B2
- Status: Granted
- Kind: B2
- Application number: 16/140,169
- Filed: 2018-09-24
- Published: 2019-01-24
- Granted: 2020-12-22
- Earliest claimed: 2016-03-24
- Assignees: GreenMantra Recycling Technologies Ltd.
- Applicants: GreenMantra Recycling Technologies Ltd.
- Inventors: Domenic Di Mondo
- Web page: https://patentgrep.com/patent/US10870739B2

## CPC

- C08J 11/10: by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation (depolymerisation to the original monomer C07)
- C08J 3/201: {Pre-melted polymers}
- C08J 11/16: by treatment with inorganic material (C08J11/14 takes precedence)
- C08L 23/06: Polyethylene
- C08L 91/06: Waxes
- B01J 19/18: Stationary reactors having moving elements inside (B01J19/08, B01J19/26 take precedence)
- B01J 2219/0004: Processes in series
- B01J 2219/00051: Controlling the temperature
- C08J 2323/02: not modified by chemical after treatment
- C08J 2323/06: Polyethene
- C08J 2323/12: Polypropene
- C08J 2491/06: Waxes
- Y02W 30/62: Plastics recycling; Rubber recycling
- C08J: WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H (working, e.g. shaping, of plastics B29)
- C08L: COMPOSITIONS OF MACROMOLECULAR COMPOUNDS (compositions based on polymerisable monomers C08F, C08G; artificial filaments or fibres D01F; textile treating compositions D06)
- B01J: CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT

## Abstract

An improved method forms and employs a wax to modify throughputs and melt flow in polymers. The method includes: (a) selecting a solid polymeric material, (b) heating the solid polymeric material in an extruder to produce a molten polymeric material, (c) filtering the molten polymeric material, (d) placing the molten polymeric material through a chemical depolymerization process in a reactor to produce a depolymerized polymeric material, and (e) adding the depolymerized material to a pre-wax mixture to produce a modified polymer.

## Claims

### Claim 1

A method for forming a depolymerized wax and employing said depolymerized wax to modify polymeric processing and material properties, the method comprising:
selecting a solid polymeric post-consumer or post-industrial feed;
heating said solid polymeric post-consumer or post-industrial feed in an extruder to produce a molten polymeric material;
filtering said molten polymeric material;
placing said molten polymeric material through a chemical depolymerization process in a reactor to produce a depolymerized wax material, wherein the depolymerized wax material has a melting point between 106° C. and 135° C.;
adding said depolymerized wax material into a pre-wax mixture to produce a modified polymer with an increased melt flow index, wherein said pre-wax material comprises a polymer.

### Claim 2 (depends on 1)

The method of claim 1, wherein said method is continuous or semi-continuous.

### Claim 3 (depends on 1)

The method of claim 1, further comprising:
filtering said solid polymeric post-consumer or post-industrial feed.

### Claim 4 (depends on 1)

The method of claim 1, further comprising:
cooling said depolymerized wax material.

### Claim 5 (depends on 4)

The method of claim 4, further comprising:
purifying said depolymerized wax material.

### Claim 6 (depends on 5)

The method of claim 5, wherein said purifying step employs one of flash separation, absorbent beds, clay polishing and film evaporators.

### Claim 7 (depends on 1)

The method of claim 1, wherein said depolymerized wax material is added to said pre-wax mixture via an in-line pump.

### Claim 8 (depends on 3)

The method of claim 3, wherein said filtering step employs a filter bed.

### Claim 9 (depends on 1)

The method of claim 1, wherein said depolymerization process employs a catalyst.

### Claim 10 (depends on 9)

The method of claim 9, wherein said catalyst is supported on zeolite or alumina.

### Claim 11 (depends on 1)

The method of claim 1, wherein said depolymerization process employs a second reactor.

### Claim 12 (depends on 11)

The method of claim 11, wherein said reactors are connected in series.

### Claim 13 (depends on 11)

The method of claim 11, wherein said reactors are stacked vertically.

### Claim 14 (depends on 1)

The method of claim 1, wherein said reactor comprises a static mixer.

### Claim 15 (depends on 1)

The method of claim 1, wherein said solid polymeric post-consumer or post-industrial feed includes recycled polyethylene.

### Claim 16 (depends on 1)

The method of claim 1, wherein solid polymeric post-consumer or post-industrial feed includes recycled polypropylene.

### Claim 17 (depends on 1)

The method of claim 1, wherein said solid polymeric post-consumer or post-industrial feed includes inorganics.

### Claim 18 (depends on 1)

The method of claim 1, wherein the amount of said depolymerized wax material mixed into said pre-wax mixture is between 1 to 5 percent of the weight of said modified polymer.

### Claim 19

A method for forming a depolymerized wax and employing said depolymerized wax to modify polymeric processing and material properties, the method comprising:
selecting a solid polymeric post-consumer or post-industrial feed;
heating said solid polymeric post-consumer or post-industrial feed in an extruder to produce a molten polymeric material;
filtering said molten polymeric material;
placing said molten polymeric material through a chemical
depolymerization process hi a reactor to produce a depolymerized wax material, wherein the depolymerized wax material has a melting point between 106° C. and 135° C.;
adding said depolymerized wax material into a pre-wax mixture to produce a modified polymer with an increased melt flow index, wherein said pre-wax mixture comprises said solid polymeric post-consumer or post-industrial feed which has not been depolymerized.

### Claim 20

A method for forming a depolymerized wax and employing said depolymerized wax to modify polymeric processing and material properties, the method comprising:
selecting a solid polymeric post-consumer or post-industrial feed, wherein said solid polymeric post-consumer or post-industrial feed comprises recycled polyethylene and inorganics;
heating said solid polymeric post-consumer or post-industrial feed in an extruder to produce a molten polymeric material;
filtering said molten polymeric material;
placing said molten polymeric material through a chemical depolymerization process in a reactor to produce a depolymerized wax material, wherein said depolymerized wax material has a melting point between 106° C. and 135° C.;
adding said depolymerized wax material into a pre-wax mixture wherein said pre-wax mixture comprises said solid polymeric post-consumer or post-industrial feed which has not been depolymerized to produce a modified polymer with an increased melt flow index,
wherein the amount of said depolymerized wax material mixed into said pre-wax mixture is between 1 to 5 percent of the weight of said modified polymer.
