US4472215A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Continuous method and apparatus for the preparation of explosives emulsion precursor
Assignee: C-I-L Inc A CORP OF CANADA
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Filing: 1983-03-24
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Granted: 1984-09-18
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Expires: 2003-03-24
Abstract
Abstract A process and apparatus is provided for the continuous manufacture of a water-in-oil explosive emulsion precursor. Separate streams of the water phase component and the oil phase component are introduced into an in-line motionless mixer. A chosen portion of the output from the mixer is recirculated and returned to the motionless mixer for further emulsification. The process allows for the production of a very high phase ratio water-to-oil emulsion (up to 95% water phase) without phase inversion after long storage. The precursor is simply converted to a sensitive explosive by means of known density lowering techniques.
Inventors
- 👤 Rejean Binet
- 👤 Chang-Hwa Chin
- 👤 Anthony C. F. Edmonds
- 👤 Ming C. Lee
- 👤 Roland Picard
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 04:57
CPC Classifications
C; C06; C06B; C06B21/00; C06B21/0008; B; B01; B01F; B01F25/00; B01F25/50; B01F25/51; C06B47/00; C06B47/14; C06B47/145
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
245 words
A continuous method for the manufacture of a water-in-oil explosive emulsion precursor wherein the ratio of discontinuous aqueous phase to continuous oil phase is at least 8 to 1 by weight, comprising the steps of: (a) forming an aqueous salt solution containing at least 75% by weight of oxygen-supplying salt, (b) forming a liquid mixture comprising a hydrocarbon fuel and an emulsifier, (c) passing a stream of said liquid fuel-emulsifier mixture into the inlet of a motionless in-line mixer, collecting said stream from the outlet of said mixer and reintroducing same through a recirculation loop into the said mixer inlet until the said recirculation loop is substantially filled with said fuel/emulsifier mixture, (d) introducing and continuously adding a stream of said aqueous salt solution to the said recirculating fuel/emulsifier mixture stream, the weight ratio of said salt solution to said fuel/emulsifier mixture being at least 8:1, and passing said salt and fuel streams through the said in-line mixer, (e) collecting at least 80% by volume of the mixed streams from the said in-line mixer outlet and reintroducing same through said recirculation loop to the said in-line mixer inlet for further mixing, and (f) withdrawing the mixed unrecirculated and recirculated streams from the said in-line mixer outlet in the form of a stable water-in-oil emulsion explosive precursor while adding an amount of liquid fuel/emulsifier mixture and an aqueous salt solution to the said in-line mixer inlet in an amount equal to the amount of emulsion withdrawn.
Claim 2
Dependent Claim
245 words
A continuous method for the manufacture of a water-in-oil explosive emulsion precursor wherein the ratio of discontinuous aqueous phase to continuous oil phase is at least 8 to 1 by weight, comprising the steps of: (a) forming an aqueous salt solution containing at least 75% by weight of oxygen-supplying salt, (b) forming a liquid mixture comprising a hydrocarbon fuel and an emulsifier, (c) passing a stream of said liquid fuel-emulsifier mixture into the inlet of a motionless in-line mixer, collecting said stream from the outlet of said mixer and reintroducing same through a recirculation loop into the said mixer inlet until the said recirculation loop is substantially filled with said fuel/emulsifier mixture, (d) introducing and continuously adding a stream of said aqueous salt solution to the said recirculating fuel/emulsifier mixture stream, the weight ratio of said salt solution to said fuel/emulsifier mixture being at least 8:1, and passing said salt and fuel streams through the said in-line mixer, (e) collecting at least 80% by volume of the mixed streams from the said in-line mixer outlet and reintroducing same through said recirculation loop to the said in-line mixer inlet for further mixing, and (f) withdrawing the mixed unrecirculated and recirculated streams from the said in-line mixer outlet in the form of a stable water-in-oil emulsion explosive precursor while adding an amount of liquid fuel/emulsifier mixture and an aqueous salt solution to the said in-line mixer inlet in an amount equal to the amount of emulsion withdrawn.
Claim 3
Dependent Claim
21 words
A method as claimed in claim 1, wherein the said salt solution is maintained at a temperature above the crystallization temperature.
Claim 4
Dependent Claim
21 words
A method as claimed in claim 1, wherein the said fuel/emulsifier mixture is formed from converging streams of fuel and emulsifier.
Claim 5
Dependent Claim
15 words
A method as claimed in claim 1, wherein the quantity of recirculating material is variable.
Claim 6
Dependent Claim
137 words
An assembly for the continuous production of a water-in-oil explosive emulsion precursor, said assembly comprising: (a) a tubular conduit having an entry end and exit end, (b) means associated with the said entry end for the delivery therein of separate streams of an aqueous salt solution phase and a liquid hydrocarbon fuel phase, (c) an in-line motionless mixer located in said conduit between the said entry and exit ends for the mixing and emulsification of said separate salt solution and liquid fuel phases, (d) a recirculating duct loop connected into said tubular conduit on either side of said motionless mixer, and (e) pump means in said recirculating duct loop adapted to recirculate a portion of said mixed salt solution and liquid fuel phases from an outlet of said motionless mixer to an inlet of said motionless mixer.
Claim 7
Dependent Claim
137 words
An assembly for the continuous production of a water-in-oil explosive emulsion precursor, said assembly comprising: (a) a tubular conduit having an entry end and exit end, (b) means associated with the said entry end for the delivery therein of separate streams of an aqueous salt solution phase and a liquid hydrocarbon fuel phase, (c) an in-line motionless mixer located in said conduit between the said entry and exit ends for the mixing and emulsification of said separate salt solution and liquid fuel phases, (d) a recirculating duct loop connected into said tubular conduit on either side of said motionless mixer, and (e) pump means in said recirculating duct loop adapted to recirculate a portion of said mixed salt solution and liquid fuel phases from an outlet of said motionless mixer to an inlet of said motionless mixer.
Claim 8
Dependent Claim
24 words
An assembly as claimed in claim 5 also containing means whereby an emulsifier may be continuously added to the said liquid hydrocarbon fuel phase.
References Cited (Backward Citations)
US4138281A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-09-18 | 1988-03-19 | 1988-09-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-09-18 | 1992-03-19 | 1992-09-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-09-18 | 1996-03-19 | 1996-09-18 | $7700.00 | Window Closed / Lapsed |