Method and system for agricultural fertigation
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
C05C-009/00
C05C-001/00
C05C-011/00
C05B-007/00
C05D-009/00
B01J-010/00
B01J-014/00
출원번호
US-0136032
(2011-07-21)
등록번호
US-8568506
(2013-10-29)
발명자
/ 주소
Miller, John C.
Miller, Deborah L.
출원인 / 주소
Miller, John C.
대리인 / 주소
Norek, Joan I.
인용정보
피인용 횟수 :
8인용 특허 :
9
초록▼
An agricultural fertigation method includes the in situ manufacture of one or more fertilizers within the irrigation upstream of the agricultural field being irrigated. Co-reactant raw materials, namely sulfuric acid, phosphoric acid, nitric acid, potassium hydroxide, urea, ammonium hydroxide, ammon
An agricultural fertigation method includes the in situ manufacture of one or more fertilizers within the irrigation upstream of the agricultural field being irrigated. Co-reactant raw materials, namely sulfuric acid, phosphoric acid, nitric acid, potassium hydroxide, urea, ammonium hydroxide, ammonia, calcium nitrate and/or magnesium nitrate, are intermixed with each other and with the stream of the flowing irrigation water. The stream of flowing irrigation water dampens the resultant dissolution and reaction exotherms. A system wherein raw materials are efficiently fed to the irrigation system main line or a side-arm reactor efficiently implements the method.
대표청구항▼
1. A system for in situ fertilizer-manufacturing fertigation of an agricultural field under the irrigation of an active agricultural irrigation system, wherein said in situ fertilizer-manufacturing fertigation includes charging a fertilizer-nutrient feedstock to said active agricultural irrigation s
1. A system for in situ fertilizer-manufacturing fertigation of an agricultural field under the irrigation of an active agricultural irrigation system, wherein said in situ fertilizer-manufacturing fertigation includes charging a fertilizer-nutrient feedstock to said active agricultural irrigation system, said active agricultural irrigation system having flowing irrigation water upstream of said agricultural field, wherein said fertilizer-nutrient feedstock is comprised of a plurality of co-reactant fertilizer-nutrient-feedstock raw materials, wherein said plurality of co-reactant fertilizer-nutrient-feedstock raw materials generate an exotherm upon intermixing with each other and with said irrigation water, said system comprising: a plurality of fertilizer-nutrient raw-material feed points open to a stream of said flowing irrigation water, wherein said plurality of feed points are sufficiently proximate each other and wherein said stream of said flowing irrigation water has sufficient flow to intermix said plurality of co-reactant fertilizer-nutrient-feedstock raw materials with each other and with said stream of said flowing irrigation water, generating at least one dissolution exotherm and at least one reaction exotherm, and wherein said stream of said irrigation water has sufficient flow to dampen said dissolution and reaction exotherms; andmeans for separately and simultaneously feeding said plurality of co-reactant fertilizer-nutrient-feedstock raw materials to said stream of said flowing irrigation water whereby treated irrigation water is formed,wherein said irrigation system includes means for irrigating said agricultural field with said treated irrigation water. 2. The system for in situ fertilizer-manufacturing fertigation of an agricultural field of claim 1 wherein said plurality of fertilizer-nutrient raw-material feed points open to a high-dilution environment. 3. The system for in situ fertilizer-manufacturing fertigation of an agricultural field of claim 1 wherein said active agricultural irrigation system includes a main line, said stream of said flowing irrigation water is flowing through said main line upstream of said agricultural field, and said plurality of feed points are disposed along said main line. 4. The system for in situ fertilizer-manufacturing fertigation of an agricultural field of claim 1 wherein said active agricultural irrigation system includes a main line and a side-arm reaction chamber off said main line, and said stream of said irrigation water is flowing through said side-arm reaction chamber and discharging to said main line, and said plurality of feed points are disposed along said side-arm reaction chamber. 5. The system for in situ fertilizer-manufacturing fertigation of an agricultural field of claim 1 further including means to regulate the feed of said plurality of co-reactant fertilizer-nutrient-feedstock raw materials being fed to said stream of said flowing irrigation water through said plurality of feed points, including means to commence said feed upon said stream reaching a first pre-selected degree of flow, means to halt said feed upon said stream reaching a second pre-selected degree of flow, and means to separately provide a pre-selected degree of feed through each of said plurality of feed points. 6. The system for in situ fertilizer-manufacturing fertigation of an agricultural field of claim 1 wherein said active agricultural irrigation system includes a main line and wherein said plurality of co-reactant fertilizer-nutrient-feedstock raw materials, upon co-reacting and upon intermixing with said flowing irrigation water, convert said irrigation water downstream of said plurality of feed points to treated irrigation water, further including means to determine the pH of said treated irrigation water upstream of said agricultural field. 7. The system for in situ fertilizer-manufacturing fertigation of an agricultural field of claim 1 further including a plurality of storage tanks and a plurality of feed lines, each feed line separately running between one of said storage tanks and one of said feed points. 8. The system for in situ fertilizer-manufacturing fertigation of an agricultural field of claim 1 wherein said feed points are spaced apart a maximum of ten inches. 9. A method of in situ fertilizer-manufacturing fertigation of an agricultural field, said agricultural field being irrigated by means of an active irrigation system having flowing irrigation water upstream of said agricultural field, said method comprising the steps of: (step 1) manufacturing a fertilizer in situ by charging a fertilizer-nutrient feedstock comprised of co-reactant fertilizer-nutrient-feedstock raw materials to said active agricultural irrigation system by sub-steps 1a and 1b of(sub-step 1a) charging a first fertilizer-nutrient-feedstock raw material to a stream of said flowing irrigation water upstream of said agricultural field at a first feed point;(sub-step 1b) simultaneously charging a second fertilizer-nutrient-feedstock raw material exothermically co-reactant with said first fertilizer-nutrient-feedstock raw material to said stream of flowing irrigation water at a second feed point,wherein said first and second fertilizer-nutrient-feedstock raw materials are selected from the group consisting of sulfuric acid, phosphoric acid, nitric acid, potassium hydroxide, urea, ammonium hydroxide, ammonia, calcium nitrate and magnesium nitrate,wherein said first and second feed points are sufficiently proximate each other and wherein said stream of flowing irrigation water has sufficient flow to intermix said first and said second fertilizer-nutrient-feedstock raw materials with each other and with said irrigation water, generating at least one dissolution exotherm and at least one reaction exotherm, andwherein said stream of flowing irrigation water has sufficient flow to dampen said dissolution and reaction exotherms,whereby said irrigation water is converted to treated irrigation water; and(step 2) irrigating said agricultural field with said treated irrigation water. 10. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9 wherein said flow of said stream of flowing irrigation water is sufficient to dampen said dissolution and reaction exotherms to a maximum temperature increase of 40 degrees F. over ambient irrigation water temperature. 11. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9 wherein said flow of said stream of flowing irrigation water is sufficient to dampen said dissolution and reaction exotherms to a maximum temperature increase of 20 degrees F. over ambient irrigation water temperature. 12. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9 wherein, in sub-steps 1a and 1b, said simultaneous charging of said first and second fertilizer-nutrient-feedstock raw materials to said stream of flowing irrigation water is a charging of said first and second fertilizer-nutrient-feedstock raw materials to a high-dilution environment. 13. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9 wherein said agricultural irrigation system includes a main line upstream of said agricultural field, and wherein, in sub-steps 1a and 1b, said charging of said first and second fertilizer-nutrient-feedstock raw materials to said stream of flowing irrigation water is a charging of said first and second fertilizer-nutrient-feedstock raw materials to said main line. 14. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9, wherein said agricultural irrigation system includes a main line upstream of said agricultural field and a side-arm reaction chamber off said main line, wherein said stream of flowing irrigation water is flowing through said side-arm reaction chamber and discharging to said main line, and wherein, in sub-steps 1a and 1b, said first and second fertilizer-nutrient-feedstock raw materials are charged to said stream of said irrigation water flowing through said side-arm reaction chamber. 15. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9, wherein said manufactured-in-situ fertilizer is among the group consisting of potassium nitrate, potassium sulfate, potassium hydrogen sulfate, potassium ammonium sulfate, potassium phosphate (mono-H), potassium phosphate (di-H), potassium phosphate, potassium ammonium phosphate (mono-K and mono-NH4), potassium ammonium phosphate (di-K and mono-NH4), potassium ammonium phosphate (mono-K and di-NH4), urea nitrate, urea phosphate, dicarbamide dihydrogen sulfate, monocarbamide dihydrogen sulfate, urea ammonium nitrate, ammonium nitrate, ammonium sulfate, ammonium hydrogen sulfate, ammonium phosphate (mono-H), ammonium phosphate (di-H), ammonium phosphate, calcium ammonium nitrate and magnesium ammonium nitrate. 16. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9, wherein said first and second fertilizer-nutrient-feedstock raw materials are sulfuric acid and potassium hydroxide. 17. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9, wherein said first fertilizer-nutrient-feedstock raw material is sulfuric acid in an aqueous solution containing from 50 to 98 wt. percent sulfuric acid and said second fertilizer-nutrient-feedstock raw material is selected from the group consisting of potassium hydroxide as a 35 to 50 wt. percent aqueous solution, urea as a 40 to 50 wt. percent aqueous solution, ammonium hydroxide as a 20 to 29 wt. percent aqueous solution and ammonia as a 95 to 100 wt. percent gas. 18. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9, wherein said first fertilizer-nutrient-feedstock raw material is nitric acid in an aqueous solution containing from 50 to 71 wt. percent nitric acid and said second fertilizer-nutrient-feedstock raw material is selected from the group consisting of potassium hydroxide as a 35 to 50 wt. percent aqueous solution, urea as a 40 to 50 wt. percent aqueous solution, ammonium hydroxide as a 20 to 29 wt. percent aqueous solution and ammonia as a 95 to 100 wt. percent gas. 19. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9, wherein said first fertilizer-nutrient-feedstock raw material is phosphoric acid in an aqueous solution containing from 65 to 85 wt. percent phosphoric acid and said second fertilizer-nutrient-feedstock raw material is selected from the group consisting of potassium hydroxide as a 35 to 50 wt. percent aqueous solution, urea as a 40 to 50 wt. percent aqueous solution, ammonium hydroxide as a 20 to 29 wt. percent aqueous solution and ammonia as a 95 to 100 wt. percent gas. 20. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9, further including in step 1 the sub-step 1c of: (sub-step 1c) simultaneously charging a third fertilizer-nutrient-feedstock raw material exothermically co-reactant with said first and said second fertilizer-nutrient-feedstock raw material to said stream of said irrigation water at a third feed point,wherein said first, second and third feed points are sufficiently proximate each other and wherein said stream of said irrigation water has sufficient flow to exothermically intermix said first, second and third fertilizer-nutrient-feedstock raw materials with each other and with said irrigation water, generating at least one dissolution exotherm and at least one reaction exotherm. 21. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 9, further including the steps of: selecting a target pH;determining the pH of said treated irrigation water; andcharging an acid to said stream of flowing irrigation water in an amount sufficient to adjust said pH of said treated irrigation water to a target pH. 22. A method of in situ fertilizer-manufacturing fertigation of an agricultural field under the irrigation of an active agricultural irrigation system, including feeding a fertilizer-nutrient feedstock to said active agricultural irrigation system, using the in situ fertilizer-manufacturing fertigation system of claim 1, said active agricultural irrigation system having flowing irrigation water upstream of said agricultural field, said in situ fertilizer-manufacturing fertigation system having a plurality of fertilizer-nutrient raw-material feed points opening to a stream of said flowing irrigation water, wherein said plurality of feed points are sufficiently proximate each other and wherein said stream of said irrigation water has sufficient flow to intermix said plurality of co-reactant fertilizer-nutrient-feedstock raw materials with each other and with said stream of said flowing irrigation water, generating at least one dissolution exotherm and at least one reaction exotherm, and wherein said stream of flowing irrigation water has sufficient flow to dampen said dissolution and reaction exotherms, and means for separately and simultaneously feeding said plurality of co-reactant fertilizer-nutrient-feedstock raw materials to said stream of said flowing irrigation water whereby treated irrigation water is formed, wherein said agricultural irrigation system includes means for irrigating said agricultural field with said treated irrigation water, said method comprising the steps of: (step 1) manufacturing a fertilizer in situ by simultaneously feeding said plurality of co-reactant fertilizer-nutrient-feedstock raw materials to said stream of flowing irrigation water, whereby said irrigation water is converted to treated irrigation water,wherein said plurality of co-reactant fertilizer-nutrient-feedstock raw materials are selected from the group consisting of sulfuric acid, phosphoric acid, nitric acid, potassium hydroxide, urea, ammonium hydroxide, ammonia, calcium nitrate and magnesium nitrate; and(step 2) irrigating said agricultural field with said treated irrigation water. 23. The method of in situ fertilizer-manufacturing fertigation of an agricultural field system of claim 22 wherein said plurality of fertilizer-nutrient-feedstock raw-material feed points open to a high-dilution environment, and wherein, in said step 1, said simultaneously feeding said plurality of co-reactant fertilizer-nutrient-feedstock raw materials to said stream of flowing irrigation water is simultaneously feeding to said high-dilution environment. 24. The method of in situ fertilizer-manufacturing fertigation of an agricultural field system of claim 22 wherein said active agricultural irrigation system includes a main line, said stream of said flowing irrigation water is flowing through said main line upstream of said agricultural field, said plurality of feed points are disposed along said main line, and wherein, in said step 1, said simultaneously feeding said plurality of co-reactant fertilizer-nutrient-feedstock raw materials to said stream of flowing irrigation water is simultaneously feeding to said main line. 25. The method of in situ fertilizer-manufacturing fertigation of an agricultural field system of claim 22 wherein said active agricultural irrigation system includes a main line and a side-arm reaction chamber off said main line, and said stream of flowing irrigation water is flowing through said side-arm reaction chamber and discharging to said main line, said plurality of feed points are disposed along said side-arm reaction chamber, and wherein, in said step 1, said simultaneously feeding said plurality of co-reactant fertilizer-nutrient-feedstock raw materials to said stream of flowing irrigation water is simultaneously feeding to said side-arm reaction chamber. 26. The method of in situ fertilizer-manufacturing fertigation of an agricultural field system of claim 22 wherein said system further includes means to regulate the feed of said plurality of co-reactant fertilizer-nutrient-feedstock raw materials being fed to said stream of said flowing irrigation water through said plurality of feed points, including means to commence said feed upon said stream reaching a first pre-selected degree of flow, means to halt said feed upon said stream reaching a second pre-selected degree of flow, and means to separately provide a pre-selected degree of feed through each of said plurality of feed points, wherein, in said step 1, said simultaneous feeding of said plurality of co-reactant fertilizer-nutrient-feedstock raw materials commences upon said stream reaching a first pre-selected degree of flow, halts upon said stream reaching a second pre-selected degree of flow, and is at a pre-selected degree of feed through each of said plurality of feed points. 27. The method of in situ fertilizer-manufacturing fertigation of an agricultural field system of claim 22 further including the steps of determining and adjusting the pH of said treated irrigation water upstream of said agricultural field. 28. The method of in situ fertilizer-manufacturing fertigation of an agricultural field system of claim 22 wherein said system further includes a plurality of storage tanks and a plurality of feed lines, each feed line separately running between one of said storage tanks and one of said feed points, further including the step of separately feeding said plurality of co-reactant fertilizer-nutrient-feedstock raw materials from said plurality of storage tanks to and through said feed lines to said feed points. 29. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 22, wherein said manufactured-in-situ fertilizer is among the group consisting of potassium nitrate, potassium sulfate, potassium hydrogen sulfate, potassium ammonium sulfate, potassium phosphate (mono-H), potassium phosphate (di-H), potassium phosphate, potassium ammonium phosphate (mono-K and mono-NH4), potassium ammonium phosphate (di-K and mono-NH4), potassium ammonium phosphate (mono-K and di-NH4), urea nitrate, urea phosphate, dicarbamide dihydrogen sulfate, monocarbamide dihydrogen sulfate, urea ammonium nitrate, ammonium nitrate, ammonium sulfate, ammonium hydrogen sulfate, ammonium phosphate (mono-H), ammonium phosphate (di-H), ammonium phosphate, calcium ammonium nitrate and magnesium ammonium nitrate. 30. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 22, wherein said plurality of fertilizer-nutrient-feedstock raw materials are sulfuric acid and potassium hydroxide. 31. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 22, wherein said plurality of fertilizer-nutrient-feedstock raw materials are sulfuric acid in an aqueous solution containing from 50 to 98 wt. percent sulfuric acid and a fertilizer-nutrient-feedstock raw material selected from the group consisting of potassium hydroxide as a 35 to 50 wt. percent aqueous solution, urea as a 40 to 50 wt. percent aqueous solution, ammonium hydroxide as a 20 to 29 wt. percent aqueous solution and ammonia as a 95 to 100 wt. percent gas. 32. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 22, wherein said plurality of fertilizer-nutrient-feedstock raw materials are nitric acid in an aqueous solution containing from 50 to 71 wt. percent nitric acid and a fertilizer-nutrient-feedstock raw material selected from the group consisting of potassium hydroxide as a 35 to 50 wt. percent aqueous solution, urea as a 40 to 50 wt. percent aqueous solution, ammonium hydroxide as a 20 to 29 wt. percent aqueous solution and ammonia as a 95 to 100 wt. percent gas. 33. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 22, wherein said plurality of fertilizer-nutrient-feedstock raw materials are phosphoric acid in an aqueous solution containing from 65 to 85 wt. percent phosphoric acid and a fertilizer-nutrient-feedstock raw material selected from the group consisting of potassium hydroxide as a 35 to 50 wt. percent aqueous solution, urea as a 40 to 50 wt. percent aqueous solution, ammonium hydroxide as a 20 to 29 wt. percent aqueous solution and ammonia as a 95 to 100 wt. percent gas. 34. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 22 wherein said flow of said stream of flowing irrigation water is sufficient to dampen said dissolution and reaction exotherms to a maximum temperature increase of 40 degrees F. over ambient irrigation water temperature. 35. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 22 wherein said flow of said stream of flowing irrigation water is sufficient to dampen said dissolution and reaction exotherms to a maximum temperature increase of 20 degrees F. over ambient irrigation water temperature. 36. The method of in situ fertilizer-manufacturing fertigation of an agricultural field of claim 22 wherein said feed points are spaced apart a maximum of ten inches.
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이 특허에 인용된 특허 (9)
Mazzei Angelo L. (Bakersfield CA) Wearin Jim (Fresno CA) Figgs Joseph E. (Fresno CA), Automatic controller for injection of additives into irrigation water.
McCann Ian R. (Department of Agricultural Engineering University of Idaho Moscow ID 83843) Stark Jeffrey C. (Research and Extension Center University of Idaho Aberdeen ID 83210), Method and apparatus for variable application of irrigation water and chemicals.
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