Process for preparing gum base

• US 4,459,311 A
• Filed: 01/03/1983
• Issued: 07/10/1984
• Est. Priority Date: 01/03/1983
• Status: Expired due to Term

• Current Assignee: Nabisco Technology Company
• Original Assignee: Nabisco Foods Company Limited (Mondelez International, Inc.)
• Inventors: D'Amelia, Ronald P., DeTora, Sigismondo
• Primary Examiner(s): Hunter, Jeanette M.
• Application Number:
  US06/455,152
• Time in Patent Office: 554 Days
• Field of Search: 426/3-6
• US Class Current: 426/3
• CPC Class Codes: A23G 4/02 Apparatus specially adapted for manufacture or treatment of chewing gum
• CPC Class Codes: A23G 4/04 for moulding or shaping
• CPC Class Codes: A23G 4/06 characterised by the composition containing organic or inorganic compounds
• CPC Class Codes: A23G 4/064 containing inorganic compounds
• CPC Class Codes: A23G 4/08 of the chewing gum base

Abstract

An improved process for producing gum base having a hard elastomer component by plasticizing the hard elastomer in the presence of a filler material prior to subjecting the hard elastomer to intensive mixing.

Claims

1. A process for producing gum base having a hard elastomer component comprising the steps of:

(a) blending only filler material with hard elastomer wherein the filler material is added in a weight ratio of about 15.0;

1.0 to about 1.0;

1.0 of filler material to hard elastomer, respectively, which is effective to give the hard elastomer sufficient body for further processing; and

(b) mixing a plasticizing agent with said filler-hard elastomer blend in a weight ratio of from about 0.1;

1.0 to about 3.0;

1.0 of plasticizing agent to hard elastomer, respectively, to open up said elastomer;

wherein steps (a) and (b) are completed before subjecting said plasticized blend to high intensity mixing and before adding the remainder of desired gum base components in subsequent mixing steps and the power requirement for the high intensity mixing is less than about 0.32 amps per pound of throughput at 100 r.p.m.

2. The process of claim 1 wherein said hard elastomer is in particulate form.

3. The process of claim 1 wherein said hard elastomer is selected from the group consisting of polyisobutylene, isoprene-isobutylene copolymer, and styrene-butadiene copolymer.

4. The process of claim 1 wherein said plasticizing agent is in liquid form.

5. The process of claim 1 wherein said plasticizing agent is selected from the group consisting of n-butyl stearate, oleic acid;

mono-, di-, or tri-glyceryl esters of the saturated or unsaturated fatty acids of oleic acid, caprylic acid, butyric acid, capric acid, caproic acid, lauric acid, mineral oil, liquid petroleum hydrocarbons, squalane, squalene, castor oil and other ricinoleate derivatives, diethylene or propylene glycols and derivatives, tributyl acetyl citrate, tributyl citrate, lecithin, coconut oil, glyceryl tributyrate, Zn laurate, Ca stearate, propylene glycol monostearate, propylene glycol monolaurate, fatty acids, butyl sebacate, butyl benzyl sebacate, diacetyl tartaric acid esters of mono- and diglycerides of edible fat oils or edible fat forming acids, petrolatum, stearyl monoglycerides citrate, limonene, polylimonene, natural waxes, butyl lactate, and butyl oleate.

6. The process of claim 1 wherein said elastomer is polyisobutylene and said plasticizing agent is liquid microcrystalline wax.

7. The process of claim 1 wherein said elastomer is styrene-butadiene copolymer and said plasticizer is n-butyl stearate.

8. The process of claim 1 wherein said filler material is selected from the group consisting of CaCO₃, MgCO₃, Al₂ O₃ and talc.

9. The process of claim 8 wherein said filler material is CaCO₃.

10. The process of claim 1 wherein said ratio is from about 0.25:

1.0 to about 2.00;

1.0.

11. The process of claim 10 wherein said ratio is from about 0.5:

1.0 to about 1.0;

1.0.

12. The process of claim 1 wherein said ratio is from about 8.0:

1.0 to about 2.0;

1.0.

13. The process of claim 12 wherein said ratio is about 3.0:

1.0.

14. The process of claim 1 which further comprises a continuous process wherein additional gum base components are included by a subsequent intermediate intensity mixing step, and then a high speed mixing step.

15. The process of claim 1 wherein said high intensive mixing apparatus is run at from about 60 to about 100 r.p.m. with low power requirement.

16. The process of claim 15 wherein said power requirement is not more than about 0.16 amps.