IP Library Granted Patent US 12686730
Granted Patent B2
US 12686730 · App. 18/264,880 · Granted Jul 21, 2026

Method for obtaining plastic admixture material and bioplastic material from bread waste

Inventor: Hatice Busra Koksal (Istanbul, TR)
C08B31/00C08L3/02C08L2201/06
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Quick Facts
Patent No.
US 12686730
App. No.
18/264,880
Granted
Jul 21, 2026
Kind
B2
Abstract

In the relevant technical field, cellulose-based wastes or agricultural wastes are used as raw materials in the production of environmentally friendly bioplastics or plastic admixture materials. The cost spent on a product is high to recycle agricultural wastes into these said final products. In addition, cellulose-based raw materials such as olive seeds are not as suitable for polymerization as starches. In this context, in the invention, starch-based bread waste is used as a raw material for the production of bioplastics and plastic admixture materials. The bread wastes are more suitable for polymerization, and when used as raw material, the product price per unit time is more economical compared to other agricultural or waste foodstuffs.

Claims (30)

1 . The production method of bioplastics and/or plastic admixture materials, characterized in that it includes the process steps of;

cutting bread waste by slicing and allowing to dry,

bringing the bread wastes into powder form by grinding process after the drying process,

obtaining waste bread powder:water mixture by adding water to bread waste in powder form and dissolving,

adding HCl with a concentration of at least 30% to the waste bread powder:water mixture,

by adding HCl, releasing the starches in the powdered bread waste, and then by adding glycerin, achieving the polymerization, and obtaining the mixture containing bio-raw material,

adding NaOH neutralizing the mixing medium,

adding sodium metabisulphite-water solution to the mixture and then allowing the mixture to dry,

reducing the dimension of the dried bio-raw material by grinding,

mixing the resulting bio-raw materials by subjecting to the twin screw extruder process and adding maleic anhydride and an antioxidant as an additional component and obtaining bioplastic as a result of the processes.

2 . A production method according to claim 1 , characterized in that it includes the process steps of;

Mixing powdered bread waste in water at a value between 1/1 and 2/1 (w/v) (g/mL),

adding HCl with a concentration of at least 30% at a value between 1/10 (v/v) and 7/10 (v/v) to the resulting powdered bread waste:water mixture,

adding glycerine to the mixture in a value between 2/10 (v/v) and 15/10 (v/v) of the water amount,

adding a NaOH solution at a ratio between 2/10 (v/v) and 7/10 (v/v) in the mixture,

adding sodium metabisulphite solution to the bio-raw material mixture at a value between 1/10 and 5/10 of the amount of added water,

allowing the mixture to dry for 24 to 72 hours,

performing the twin screw extruder mixing process of the bio-raw material at a maximum temperature of 250° C. and obtaining bioplastic by adding 0.5-2% of maleic anhydride and 0.5%-2% of antioxidant from the side feeder during the process.

3 . A production method according to claim 1 , characterized in that the waste bread powder:water mixture is between 1.2:1 and 1.8:1 (g:mL).

4 . A production method according to claim 3 , characterized in that the waste bread powder:water mixture is 1.5:1 (g:mL).

5 . A production method according to claim 1 , characterized in that the said HCl is added at the ratios between 2/10 (v/v) and 7/10 (v/v) to the waste bread powder:water mixture.

6 . A production method according to claim 1 , characterized in that the said amount of glycerin is added at a value between 4/10 (v/v) and 12/10 (v/v) of the water amount in the mixture.

7 . A production method according to claim 1 , characterized in that the said amount of NaOH is between 4/10 (v/v) and 6/10 (v/v) in the mixture.

8 . A production method according to claim 1 , characterized in that the said drying process is performed for a period of 48 hours.

9 . A production method according to claim 2 , characterized in that the waste bread powder:water mixture is between 1.2:1 and 1.8:1 (g:mL).

10 . A production method according to claim 9 , characterized in that the waste bread powder:water mixture is 1.5:1 (g:mL).

11 . A production method according to claim 2 , characterized in that the said HCI is added at the ratios between 2/10 (v/v) and 7/10 (v/v) to the waste bread powder:water mixture.

12 . A production method according to claim 2 , characterized in that the said amount of glycerin is added at a value between 4/10 (v/v) and 12/10 (v/v) of the water amount in the mixture.

13 . A production method according to claim 2 , characterized in that the said amount of NaOH is between 4/10 (v/v) and 6/10 (v/v) in the mixture.

14 . A production method according to claim 2 , characterized in that the said drying process is performed for a period of 48 hours.