Controlled bulk vegetable fermentation

• US 3,932,674 A
• Filed: 11/29/1974
• Issued: 01/13/1976
• Est. Priority Date: 11/29/1974
• Status: Expired due to Term

• Current Assignee: Government of the United States of America
• Original Assignee: Government of the United States of America
• Inventors: Thompson, Roger L., Fleming, Henry P., Bell, Thomas A., Etchells, John L.
• Primary Examiner(s): Monacell, A. Louis
• Assistant Examiner(s): Massung, Esther L.
• Application Number:
  US05/528,454
• Time in Patent Office: 410 Days
• Field of Search: 426/49, 426/52
• US Class Current: 426/52
• CPC Class Codes: A23B 7/10 Preserving with acids; Acid fermentation

Abstract

Bulk fermentation of brined vegetables comprising controlled sanitizing, acidifying, buffering, and inoculating while continually purging CO₂ from the fermenting vegetable/brine mass.A non-exclusive, irrevocable, royalty-free license in the invention herein described, throughout the world for all purposes of the United States Government, with the power to grant sublicenses for such purposes, is hereby granted to the Government of the United States of America.

Claims

1. A rapid, controlled bulk fermentation process for vegetables, under conventional pack-out conditions, which comprises washing said vegetables and then immersing them in a 15°

-32°

salometer brine;

further sanitizing the resulting vegetable/brine mass by chlorinating and acidifying the brine to the extent necessary to provide, respectively, from about 50 to about 100 parts per million of active chlorine in the brine and a pH thereof between about 2.7 and about 3.2, said chlorine destroying substantially all the microflora in the brine;

maintaining initial brine strengths by counteracting dilution of the brine resulting from diffusion of vegetable moisture by incrementally adding salt to the brine until the point of near equilibration, the brine at that point containing between about 0.2 and about 0.6% sugar, by volume;

repeating the chlorine sanitizing step at least once about midway between the original chlorination and equilibration to again destroy microflora build-up in the brine;

uniformly buffering the nutrient-containing brine to a pH between about 4.2 and 4.8;

then adding to said brine a viable culture of one or more species of lactic acid bacteria either singly or in conjunction;

sweeping with an inert gas autogenously-produced CO₂ from the brine during the above steps, this purging being carried out until fermentation is essentially complete, i.e., when the sugar content of the vegetable/brine mass is near zero and there is essentially no further development of brine acid; and

the above process being carried out at a temperature in the range of about 65°

F. to about 90°

F.

2. The process of claim 1 wherein cucumbers are the vegetables.

3. The process of claim 2 wherein the acidifying agent is acetic acid.

4. The process of claim 3 wherein the buffer is sodium acetate.

5. The process of claim 4 wherein the lactic acid bacteria species is a combination of Lactobacillus plantarum and Pediococcus cerevisiae.

6. The process of claim 5 wherein the inert sweeping gas is nitrogen.

7. The process of claim 6 wherein the pack-out ratio is in the range, by volume, of about 40 to about 75 percent vegetable to about 60 to about 25 percent brine.

8. The process of claim 7 wherein the salt concentration is in the range of 20°

-28°

salometer;

the active chlorine concentration is in the range of about 70 to about 90 ppm;

the sugar concentration of the brine at or near equilibration is in the range of about 0.4 and about 0.6 percent, by volume;

the pH of the brine upon buffering is in the range of about 4.5 to about 4.7;

the temperature of the cucumber/brine mass is in the range of 78°

-85°

F.;

the pack-out ratio is in the range of about 55 to about 70 cucumbers to about 45 to about 30 brine; and

no. 3 grade size cucumbers are the vegetables.

9. The process of claim 8 wherein sweeping of autogenously-produced CO₂ out of the cucumber/brine mass is effected by introducing gaseous nitrogen at the bottom of the fermentation zone containing said mass and allowing it to rise through the zone and sweep the dissolved CO₂ along with it and upwardly through the zone and out the top thereof, the quantity and rate of flow of the gaseous nitrogen being sufficient to reduce the CO₂ content and pressure below that at which it can deleteriously affect the final brine-stock product.

10. The process of claim 9 wherein small-sized cucumbers having a diameter of 11/4 inches or less are the vegetable, in lieu of grade size no. 3 cucumbers, and the initial cover brine containing chlorine is drained off after about 36 to about 48 hours, the stock re-brined, chlorinated, acidified, and the fermentation process completed.