국가/구분 |
United States(US) Patent
등록
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국제특허분류(IPC7판) |
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출원번호 |
US-0638566
(2000-08-14)
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발명자
/ 주소 |
- Gutwein, Roger William
- Connor, Christopher Wade
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출원인 / 주소 |
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대리인 / 주소 |
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인용정보 |
피인용 횟수 :
26 인용 특허 :
82 |
초록
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An improved process for providing an individually customized fresh brewed coffee beverage on demand by a consumer, in a wide range of variety and strength. Said brewing process for making relatively large quantities of fresh brewed coffee beverages (in particular customized as to desired variety, bo
An improved process for providing an individually customized fresh brewed coffee beverage on demand by a consumer, in a wide range of variety and strength. Said brewing process for making relatively large quantities of fresh brewed coffee beverages (in particular customized as to desired variety, body, character and/or strengths) as chosen by multiple individual consumers just prior to their consumption, with the system being easy to use by the consumer or other individual (i.e., restaurant wait staff) obtaining the customized beverage. Further, maintenance of the equipment requires only a small amount of personal attention by the owner/operator of the equipment. “Delayed dilution” of a concentrated extract to provide a beverage brewing system which immediately (upon customer selection) provides selective dilution (based on individual consumer's selections) of a fresh brewed coffee extract after the extract has been allowed to brew and held as an extract before dilution.
대표청구항
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An improved process for providing an individually customized fresh brewed coffee beverage on demand by a consumer, in a wide range of variety and strength. Said brewing process for making relatively large quantities of fresh brewed coffee beverages (in particular customized as to desired variety, bo
An improved process for providing an individually customized fresh brewed coffee beverage on demand by a consumer, in a wide range of variety and strength. Said brewing process for making relatively large quantities of fresh brewed coffee beverages (in particular customized as to desired variety, body, character and/or strengths) as chosen by multiple individual consumers just prior to their consumption, with the system being easy to use by the consumer or other individual (i.e., restaurant wait staff) obtaining the customized beverage. Further, maintenance of the equipment requires only a small amount of personal attention by the owner/operator of the equipment. “Delayed dilution” of a concentrated extract to provide a beverage brewing system which immediately (upon customer selection) provides selective dilution (based on individual consumer's selections) of a fresh brewed coffee extract after the extract has been allowed to brew and held as an extract before dilution. a partial vacuum.14. The method of claim 1, in which the substantially liquid agricultural byproduct is condensed by being heated at a temperature between about 100 and 240 degrees Fahrenheit in a partial vacuum.15. The method of claim 1, in which the substantially liquid agricultural byproduct is condensed by being heated at a temperature between about 160 and 180 degrees Fahrenheit in a partial vacuum between about 20 and 25 inches Hg.16. The method of claim 1, further comprising blending an exogenous carbohydrate or an exogenous fat with the substantially liquid agricultural product before the solidifying step.17. The method of claim 1, further comprising blending the substantially liquid agricultural byproduct with an exogenous carbohydrate and an exogenous fat.18. The method of claim 17, further comprising blending an exogenous nitrogen source to said blend of substantially liquid agricultural byproduct, exogenous carbohydrate, and exogenous fat.19. The method of claim 17, further comprising blending vitamins and minerals to said blend of the substantially liquid agricultural byproduct, exogenous carbohydrate, and exogenous fat.20. The method of claim 1, further comprising blending a sulfonated lignin material to the substantially liquid agricultural byproduct.21. An amorphous solid cast feed product, comprising a condensed and mold-solidified substantially liquid agricultural byproduct, in which a 10 weight percent aqueous solution of the amorphous solid cast feed product has a pH less than about 7.5. 22. The amorphous solid cast feed product of claim 21, the condensed substantially liquid agricultural byproduct having a solids content of between about 71 and 97 weight percent.23. The amorphous solid cast feed product of claim 21, further comprising an exogenous fat or an exogenous carbohydrate solidified with the condensed substantially liquid agricultural byproduct.24. The amorphous solid cast feed product of claim 21, further comprising an exogenous fat and an exogenous carbohydrate solidified with the condensed substantially liquid agricultural byproduct.25. The amorphous solid cast feed product of claim 24, in which the condensed substantially liquid agricultural byproduct is selected from steepwater, condensed fermented corn extractives, stillage, condensed distillers solubles, whey, condensed whey solubles, and any mixture thereof.26. The amorphous solid cast feed product of claim 24, in which the condensed substantially liquid agricultural byproduct is selected from condensed fermented corn extractives, condensed distillers solubles, and any mixture thereof.27. The amorphous solid cast feed product of claim 26, further comprising an exogenous protein source.28. The amorphous solid cast feed product of claim 26, further comprising vitamins and minerals.29. The amorphous solid cast feed product of claim 26, further comprising a sulfonated lignin material.30. An amorphous solid cast feed product formed by a process comprising: condensing a substantially liquid agricultural byproduct; andsolidifying the condensed substantially liquid agricultural byproduct in a mold, in which a 10 weight percent aqueous solution of the amorphous solid cast feed product has a pH less than about 7.5.31. The amorphous solid cast feed product formed by the process of claim 30, in which the substantially liquid agricultural byproduct is condensed and solidified such that the amorphous solid cast feed product has a solids content between about 71 and 97 weight percent.32. The amorphous solid cast feed product formed by the process of claim 31, in which the condensed and solidified substantially liquid agricultural byproduct is selected from steepwater, condensed fermented corn extractives, stillage, condensed distillers solubles, whey, condensed whey solubles, and any mixture thereof.33. The amorphous solid cast feed product formed by the process of claim 31, in which the condensed and solidified substan tially liquid agricultural byproduct is selected from condensed fermented corn extractives, condensed distillers solubles, and any mixture thereof.34. The amorphous solid cast feed product formed by the process of claim 33, said process further comprising blending an exogenous fat or an exogenous carbohydrate with the substantially liquid agricultural byproduct.35. The amorphous solid cast feed product formed by the process of claim 33, said process further comprising blending an exogenous fat and an exogenous carbohydrate with the substantially liquid agricultural byproduct.36. The amorphous solid cast feed product formed by the process of claim 35, said process further comprising blending an exogenous nitrogen source, a vitamin, a mineral, a sulfonated lignin material a recycled animal waste product, or any combination thereof with said exogenous fat, exogenous carbohydrate, and substantially liquid agricultural byproduct.37. The amorphous solid cast feed product formed by the process of claim 30, in which the condensing step comprises heating the substantially liquid agricultural byproduct.38. The amorphous solid cast feed product formed by the process of claim 37, in which the substantially liquid agricultural byproduct is condensed by being heated at a temperature between about 100 and 240 degrees Fahrenheit.39. The amorphous solid cast feed product formed by the process of claim 30, in which the condensing step comprises heating the substantially liquid agricultural byproduct in a partial vacuum.40. The amorphous solid cast feed product formed by the process of claim 39, in which the substantially liquid agricultural byproduct is heated at a temperature between about 160 and 180 degrees Fahrenheit.41. The amorphous solid cast feed product formed by the process of claim 40, in which the partial vacuum is between about 20 and 25 inches Hg.
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