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US3843823A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of removing undesirable solids from coffee extract

Assignee: General Foods Inc
•
Filing: 1970-05-21
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Granted: 1974-10-22
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Expires: 1990-05-21
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Abstract

Abstract Coffee extract obtained by percolation is run through a filter capable or removing all visible sediment and organic matter and of reducing bacteria and other microscopic organic material to a high degree. Such a filter is, for example, of the medium duty type used for water systems, such as, public, semipublic or private swimming pools. A pair of filters are provided to permit one to be cleaned while the other is in service. This removes all visible matter and highly reduces microscopic matter in the extract (including nuclei for agglomeration of waxes and tars) which might clog downstream freezing apparatus, such as, crystallizers. Remaining insoluble solids which might form dark specks are removed by clarification in a disludging type centrifuge after freeze concentration and preliminary to freezing before freeze drying. The aforementioned filtration is accomplished at relatively high temperatures, such as from 190* to 215* F, and the centrifugal clarification at about normal ambient temperatures, such as from about 50* to 80* F and more usually between 60* to 70* F. The overall process provides a pleasantly colored product free of discoloring specks.

Inventors

  • 👤 R Chaplow
  • 👤 R Hodgman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 23:00
CPC Classifications
A; A23; A23F; A23F5/00; A23F5/24; A23F5/28; A23F5/30; A23F5/16; A23F5/18

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 93 words
A METHOD OF REMOVING UNDESIRABLE SOLIDS FROM COFFEE EXTRACT COMPRISING THE STEPS OF OBTAINING COFFEE EXTRACT, FILTERING SAID EXTRACT IN A MEDIUM DUTY FILTER TO REMOVE VISIBLE SEDIMENT AND ORGANIC MATERIAL AND TO HIGHLY REDUCE MICROSCOPIC INSOLUBLES, REDUCING THE TEMPERATURE OF THE FILTERED EXTRACT, FREEZE CONCENTRATION EXTRACT TO BETWEEN 50*-80*F ING SAID CONCENTRATED EXTRACT TO BETWEEN 50*-80*F AND CLARIFYING THE HEATED CONCENTRATED EXTRACT IN A DESLUDGING-TYPE CENTRIFUGE EFFECTIVE TO REMOVE INSOLUBLES WHICH IF NOT REMOVED PRIOR TO DRYING CAUSE UNDESIRABLE BLACK SPOTS TO APPEAR AS FOREIGN MATTER IN A RECONSTITUTED CUP OF COFFEE.
Claim 2
Independent Claim 93 words
A METHOD OF REMOVING UNDESIRABLE SOLIDS FROM COFFEE EXTRACT COMPRISING THE STEPS OF OBTAINING COFFEE EXTRACT, FILTERING SAID EXTRACT IN A MEDIUM DUTY FILTER TO REMOVE VISIBLE SEDIMENT AND ORGANIC MATERIAL AND TO HIGHLY REDUCE MICROSCOPIC INSOLUBLES, REDUCING THE TEMPERATURE OF THE FILTERED EXTRACT, FREEZE CONCENTRATION EXTRACT TO BETWEEN 50*-80*F ING SAID CONCENTRATED EXTRACT TO BETWEEN 50*-80*F AND CLARIFYING THE HEATED CONCENTRATED EXTRACT IN A DESLUDGING-TYPE CENTRIFUGE EFFECTIVE TO REMOVE INSOLUBLES WHICH IF NOT REMOVED PRIOR TO DRYING CAUSE UNDESIRABLE BLACK SPOTS TO APPEAR AS FOREIGN MATTER IN A RECONSTITUTED CUP OF COFFEE.
Claim 3
Dependent Claim 18 words
A method as set forth in claim 1 wherein said filtration is accomplished at about normal percolation temperatures.
Claim 4
Dependent Claim 18 words
A method as set forth in claim 2 wherein said temperatures range approximately from 190* to 215* F.
Claim 5
Dependent Claim 19 words
A method as set forth in claim 1 wherein said filter is of the medium duty water system type.
Claim 6
Dependent Claim 21 words
A method as set forth in claim 4 wherein said filter is of the type used for filtering swimming pool water.
Claim 7
Dependent Claim 29 words
A method as set forth in claim 1 wherein said filter includes a number of filter leaves, and the flow is from outside to inside of said filter leaves.
Claim 8
Dependent Claim 25 words
A method as set forth in claim 6 wherein said filter leaves are enclosed within mesh screens and said insolubles are trapped upon said screens.
Claim 9
Dependent Claim 22 words
A method as set forth in claim 1 wherein said filtering is accomplished at pressures ranging from about 30 to 70 psig.
Claim 10
Dependent Claim 23 words
A method as set forth in claim 1 wherein said filtering is accomplished at a flow ranging from about 6 to 11 gpm.
Claim 11
Dependent Claim 18 words
A method as set forth in claim 1 wherein said clarification is accomplished in a desludging type centrifuge.
Claim 12
Dependent Claim 21 words
A method as set forth in claim 10 wherein said clarification is accomplished at temperatures between about 50* and 80* F.
Claim 13
Dependent Claim 21 words
A method as set forth in claim 10 wherein said clarification is accomplished at temperatures between about 60* to 70* F.
Claim 14
Dependent Claim 28 words
A method as set forth in claim 1 wherein the extract is freeze concentrated in a crystallizer having a residence time ranging from about 3 to 10 minutes.
Claim 15
Dependent Claim 27 words
A method as set forth in claim 1 wherein said extract is freeze concentrated in a crystallizer having a delta T of about 35* to 50* F.
Claim 16
Dependent Claim 38 words
A method as set forth in claim 1 wherein said freeze concentration involves the separation of effluent into concentrated liquid extract and ice crystals, said ice crystals being melted, concentrated and added back to said concentrated liquid extract.
Claim 17
Dependent Claim 20 words
A method as set forth in claim 1 wherein said freeze concentration employs a separating centrifuge of the basket type.
Claim 18
Dependent Claim 23 words
A method as set forth in claim 1 wherein the filtered extract is cooled to about 40* to 70* F before freeze concentration.

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1977-10-21 1978-04-22 1978-10-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1981-10-21 1982-04-22 1982-10-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1985-10-21 1986-04-22 1986-10-22 $7700.00 Window Closed / Lapsed

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