US4426322A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for the desalination of crude tall oil
Assignee: Individual
•
Filing: 1982-12-06
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Granted: 1984-01-17
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Expires: 2002-12-06
Abstract
Abstract Crude tall oil and water undergo a mass transfer at predetermined temperature and pressure values so as to remove salts from the oil. The flow of the crude oil through a collector disposed beneath an evaporator is maintained at a speed 8 to 80 times less than the trickling speed of the crude oil flowing through the evaporator. Salts are also precipitated from the crude oil by a cooling process.
Inventors
- 👤 Hermann Stage
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 15:29
CPC Classifications
C; C11; C11B; C11B13/00; C11B13/005; Y; Y02; Y02W; Y02W30/00; Y02W30/50; Y02W30/74
Claims Analysis
Total Claims: 24
Claim 1
Independent Claim
64 words
A method for removing salts from crude tall oil having said salts dissolved or emulsified therein, wherein said method comprises: providing and contacting water with said oil at a temperature above 100° C.; maintaining said oil and said water under a predetermined pressure; and effecting a mass transfer between said water and said oil such that said water remains in a liquid aggregate state.
Claim 2
Independent Claim
64 words
A method for removing salts from crude tall oil having said salts dissolved or emulsified therein, wherein said method comprises: providing and contacting water with said oil at a temperature above 100° C.; maintaining said oil and said water under a predetermined pressure; and effecting a mass transfer between said water and said oil such that said water remains in a liquid aggregate state.
Claim 3
Dependent Claim
17 words
A method according to claim 1 which further comprises effecting said mass transfer in a countercurrent process.
Claim 4
Dependent Claim
17 words
A method according to claim 2 wherein said countercurrent process further comprises a packed column countercurrent process.
Claim 5
Dependent Claim
21 words
A method according to claim 1, 2 or 3 which further comprises maintaining said temperature below 250° during said mass transfer.
Claim 6
Dependent Claim
25 words
A method according to claim 1, 2 or 3 which further comprises maintaining said temperature between 100° C. and 160° C. during said mass transfer.
Claim 7
Dependent Claim
25 words
A method according to claim 1, 2 or 3 which further comprises maintaining said temperature between 120° C. and 140° C. during said mass transfer.
Claim 8
Independent Claim
155 words
A method for removing salts from crude tall oil using a film evaporator, a liquid collector disposed below said film evaporator and a cooling device operatively associated with said liquid collector, said crude tall oil having said salts dissolved or emulsified therein, wherein said method comprises: performing a film evaporation on said crude tall oil at a predetermined trickling speed in said film evaporator; collecting said crude tall oil in a liquid state in said liquid collector; maintaining a flow speed of said crude tall oil in said liquid collector at a speed 8 to 80 times less than said predetermined trickling speed; subjecting said crude tall oil in said liquid collector to a subcooling between 1° C. to 5° C. below a boiling temperature of said crude tall oil with said cooling device; precipitating said salts from said crude tall oil in said liquid collector; and removing continuously said salts from said liquid collector.
Claim 9
Independent Claim
155 words
A method for removing salts from crude tall oil using a film evaporator, a liquid collector disposed below said film evaporator and a cooling device operatively associated with said liquid collector, said crude tall oil having said salts dissolved or emulsified therein, wherein said method comprises: performing a film evaporation on said crude tall oil at a predetermined trickling speed in said film evaporator; collecting said crude tall oil in a liquid state in said liquid collector; maintaining a flow speed of said crude tall oil in said liquid collector at a speed 8 to 80 times less than said predetermined trickling speed; subjecting said crude tall oil in said liquid collector to a subcooling between 1° C. to 5° C. below a boiling temperature of said crude tall oil with said cooling device; precipitating said salts from said crude tall oil in said liquid collector; and removing continuously said salts from said liquid collector.
Claim 10
Dependent Claim
39 words
A method according to claim 7 wherein maintaining said flow speed further comprises maintaining said flow speed of said crude tall oil in said liquid collector at a speed 20 to 40 times less than said predetermined trickling speed.
Claim 11
Dependent Claim
29 words
A method according to claim 7 or 8 wherein said subcooling further comprises subcooling between 2° C. to 3° C. below said boiling temperature of said crude tall oil.
Claim 12
Independent Claim
155 words
A method for removing salts from crude tall oil using a film evaporator, a liquid collector disposed below said film evaporator and a cooling device operatively associated with said liquid collector, said crude tall oil having said salts dissolved or emulsified therein, wherein said method comprises: performing a film evaporation on said crude tall oil at a predetermined trickling speed in said film evaporator; collecting said crude tall oil in a liquid state in said liquid collector; maintaining a flow speed of said crude tall oil in said liquid collector at a speed 8 to 80 times less than said predetermined trickling speed; subjecting said crude tall oil in said liquid collector to a subcooling between 1° C. to 5° C. below a boiling temperature of said crude tall oil with said cooling device; precipitating said salts from said crude tall oil in said liquid collector; and removing discontinuously said salts from said liquid collector.
Claim 13
Independent Claim
155 words
A method for removing salts from crude tall oil using a film evaporator, a liquid collector disposed below said film evaporator and a cooling device operatively associated with said liquid collector, said crude tall oil having said salts dissolved or emulsified therein, wherein said method comprises: performing a film evaporation on said crude tall oil at a predetermined trickling speed in said film evaporator; collecting said crude tall oil in a liquid state in said liquid collector; maintaining a flow speed of said crude tall oil in said liquid collector at a speed 8 to 80 times less than said predetermined trickling speed; subjecting said crude tall oil in said liquid collector to a subcooling between 1° C. to 5° C. below a boiling temperature of said crude tall oil with said cooling device; precipitating said salts from said crude tall oil in said liquid collector; and removing discontinuously said salts from said liquid collector.
Claim 14
Dependent Claim
39 words
A method according to claim 10 wherein maintaining said flow speed further comprises maintaining said flow speed of said crude tall oil in said liquid collector at a speed 20 to 40 times less than said predetermined trickling speed.
Claim 15
Dependent Claim
29 words
A method according to claim 10 or 11 wherein said subcooling further comprises subcooling between 2° C. to 3° C. below said boiling temperature of said crude tall oil.
Claim 16
Dependent Claim
28 words
A method according to claim 7, 8, 10 or 11 which further comprises maintaining said predetermined trickling speed at a speed between 0.2 m/sec. and 2 m/sec., inclusive.
Claim 17
Dependent Claim
28 words
A method according to claim 7, 8, 10 or 11 which further comprises maintaining said predetermined trickling speed at a speed between 0.6 m/sec. and 0.9 m/sec., inclusive.
Claim 18
Dependent Claim
32 words
A method according to claim 7, 8, 10 or 11 which further comprises maintaining said crude tall oil within said liquid collector for an average holding time between 2 to 20 minutes.
Claim 19
Dependent Claim
28 words
A method according to claim 13 which further comprises maintaining said crude tall oil within said liquid collector for an average holding time between 2 to 20 minutes.
Claim 20
Dependent Claim
28 words
A method according to claim 14 which further comprises maintaining said crude tall oil within said liquid collector for an average holding time between 2 to 20 minutes.
Claim 21
Dependent Claim
37 words
A method according to claim 15 wherein maintaining said crude tall oil within said liquid collector further comprises maintaining said crude tall oil within said liquid collector for an average holding time between 5 to 10 minutes.
Claim 22
Dependent Claim
28 words
A method according to claim 13 which further comprises maintaining said crude tall oil within said liquid collector for an average holding time between 5 to 10 minutes.
Claim 23
Dependent Claim
28 words
A method according to claim 14 which further comprises maintaining said crude tall oil within said liquid collector for an average holding time between 5 to 10 minutes.
Claim 24
Dependent Claim
107 words
A method according to claim 7, 8, 10 or 11 which further comprises: drawing said crude tall oil in a liquid state from said liquid collector; providing and contacting water with said crude tall oil drawn from said liquid collector at a temperature above 100° C.; maintaining said crude tall oil drawn from said liquid collector under a predetermined pressure; effecting a mass transfer between said water and said crude tall oil drawn from said liquid collector such that said water remains in a liquid aggregate state; and introducing said crude tall oil drawn from said liquid collector into a subsequent distillation after effecting said mass transfer.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-01-16 | 1987-07-18 | 1988-01-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-01-16 | 1991-07-18 | 1992-01-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-01-16 | 1995-07-18 | 1996-01-17 | $7700.00 | Window Closed / Lapsed |