US4479806A
Expired / Lapsed
US
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Stabilized slurry and process for preparing same
Assignee: Alfred University Research Foundation Inc
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Filing: 1983-09-16
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Granted: 1984-10-30
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Expires: 2003-09-16
Abstract
Abstract A process for preparing a carbonaceous slurry with a Brookfield viscosity of less than 5,000 centipoise when it is measured at a solids content of 70 volume percent, ambient temperature, ambient pressure, and 100 revolutions per minute, is disclosed. In the first step of this process, a specified carbonaceous compact is provided which has a certain particle size distribution, a specific surface area of from about 0.8 to about 4.0 square meters per cubic centimeter, an interstitial porosity of less than about 20 volume, and which contains at least about 5 weight percent of colloidally sized carbonaceous particles and at least 85 weight percent of particles smaller than 300 microns. In the second stage of this process, from about 60 to about 80 parts, by volume, of said carbonaceous compact is mixed with from about 20 to about 40 parts, by volume, of carrier liquid, wherein (1)at least two liquids are mixed with said carbonaceous compact, (2)at least about 90 weight percent of the total amount of liquid mixed with said carbonaceous compact is water, and (c)no more than about 10 weight percent of the total amount of liquid mixed with said carbonacoue compact is non-aqueous liquid. A carbonacecous slurry which contains from about 60-80 volume percent of carbonaceous solid material, which has a Brookfield viscosity at 70 volume percent solids of less than 5,000 centipoise, which contains said carbonaceous compact, which contains from about 20-40 volume percent of liquid wherein (1)at least two liquids are present in the slurry, (2)at least about 90 weight percent of the liquid in the slurry is water, and (3)no more than about 10 weight percent of the liquid in the slurry is non-aqueous liquid, also is disclosed.
Inventors
- 👤 James E. Funk
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 14:03
CPC Classifications
C; C21; C21B; C21B5/00; C21B5/001; C21B5/003; C21B5/004; C10; C10L; C10L1/00; C10L1/32; C10L1/326
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
370 words
A process for preparing a carbonaceous slurry which is comprised of at least about 60 volume percent of solid carbonaceous material and which has a Brookfield viscosity at a solids content of 70 volume percent, ambient temperature, and ambient pressure, of less than 5,000 centipoise, comprising the steps of: (a) providing a carbonaceous compact, wherein: 1. said compact has a specific surface area of from about 0.8 to about 4.0 square meters per cubic centimeter and an interstitial porosity of less than about 20 volume percent, 2. said compact comprises finely divided solid carbonaceous particles, 3. from about 5 to about 70 weight percent of said solid carbonaceous particles are of colloidal size, being smaller than about 3.0 microns, 4. at least about 85 weight percent of said solid carbonaceous particles in the compact have a particle size less than about 300 microns, and 5. said compact of finely divided solid carbonaceous particles has a particle size distribution substantially in accordance with the following formula: ##EQU8## wherein: (a) CPFT is the cumulative percent of said solid carbonaceous material finer than a certain specified particle size D, in volume percent; (b) k is the number of component distributions in the consist and is at least 1; (c) X j is the fractional amount of the component j in the consist, is less than or equal to 1.0, and the sum of all of the X j 's in the consist is 1.0; (d) n is the distribution modulus of fraction j and is greater than about 0.001; (e) D is the diameter of any particle in the consist and ranges from about 0.05 to about 1180 microns; (f) D s is the diameter of the particle in fraction j, measured at 1% CPFT on a plot of CPFT versus size D, is less than D L , and is greater than 0.05 microns; (g) D L is the diameter of the size modulus in fraction j, measured by sieve size or its equivalent, and is from about 10 to about 1180 microns; and (b) mixing from about 60 to about 80 parts, by volume, of said carbonaceous compact with from about 20 to about 40 parts, by volume, of liquid, wherein:
Claim 2
Dependent Claim
370 words
A process for preparing a carbonaceous slurry which is comprised of at least about 60 volume percent of solid carbonaceous material and which has a Brookfield viscosity at a solids content of 70 volume percent, ambient temperature, and ambient pressure, of less than 5,000 centipoise, comprising the steps of: (a) providing a carbonaceous compact, wherein: 1. said compact has a specific surface area of from about 0.8 to about 4.0 square meters per cubic centimeter and an interstitial porosity of less than about 20 volume percent, 2. said compact comprises finely divided solid carbonaceous particles, 3. from about 5 to about 70 weight percent of said solid carbonaceous particles are of colloidal size, being smaller than about 3.0 microns, 4. at least about 85 weight percent of said solid carbonaceous particles in the compact have a particle size less than about 300 microns, and 5. said compact of finely divided solid carbonaceous particles has a particle size distribution substantially in accordance with the following formula: ##EQU8## wherein: (a) CPFT is the cumulative percent of said solid carbonaceous material finer than a certain specified particle size D, in volume percent; (b) k is the number of component distributions in the consist and is at least 1; (c) X j is the fractional amount of the component j in the consist, is less than or equal to 1.0, and the sum of all of the X j 's in the consist is 1.0; (d) n is the distribution modulus of fraction j and is greater than about 0.001; (e) D is the diameter of any particle in the consist and ranges from about 0.05 to about 1180 microns; (f) D s is the diameter of the particle in fraction j, measured at 1% CPFT on a plot of CPFT versus size D, is less than D L , and is greater than 0.05 microns; (g) D L is the diameter of the size modulus in fraction j, measured by sieve size or its equivalent, and is from about 10 to about 1180 microns; and (b) mixing from about 60 to about 80 parts, by volume, of said carbonaceous compact with from about 20 to about 40 parts, by volume, of liquid, wherein:
Claim 3
Dependent Claim
54 words
at least two liquids are mixed with said carbonaceous compact, 2. at least about 90 weight percent of the total amount of liquid mixed with said carbonaceous compact is water, and 3. from about 0.1 to about 10 weight percent of the total amount of liquid mixed with said carbonaceous compact is non-aqueous liquid.
Claim 4
Dependent Claim
54 words
at least two liquids are mixed with said carbonaceous compact, 2. at least about 90 weight percent of the total amount of liquid mixed with said carbonaceous compact is water, and 3. from about 0.1 to about 10 weight percent of the total amount of liquid mixed with said carbonaceous compact is non-aqueous liquid.
Claim 5
Dependent Claim
12 words
The process as recited in claim 1, wherein said k is 1.
Claim 6
Dependent Claim
14 words
The process as recited in claim 2, wherein said non-aqueous liquid is organic liquid.
Claim 7
Dependent Claim
13 words
The process as recited in claim 3, wherein said carbonaceous material is coal.
Claim 8
Dependent Claim
23 words
The process as recited in claim 4, wherein said non-aqueous liquid is liquid alkane containing from about 5 to about 17 carbon atoms.
Claim 9
Dependent Claim
43 words
The process as recited in claim 4, wherein said non-aqueous liquid is a liquid petroleum fuel selected from the group consisting of number 1 fuel oil, number 2 fuel oil, number 4 fuel oil, number 5 fuel oil, and number 6 fuel oil.
Claim 10
Dependent Claim
16 words
The process as recited in claim 6, wherein said non-aqueous liquid is number 2 fuel oil.
Claim 11
Dependent Claim
28 words
The process as recited in claim 4, wherein said non-aqueous liquid is an aromatic hydrocarbon selected from the group consisting of benzene, toluene, orthoxylene, meta-xylene, para-xylene, and indene.
Claim 12
Dependent Claim
28 words
The process as recited in claim 4, wherein said non-aqueous liquid is a nitrogen liquid compound selected from the group consisting of pyridine, alpha-picoline, beta-picoline, gamma-picoline, and quinoline.
Claim 13
Dependent Claim
26 words
The process as recited in claim 4, wherein said non-aqueous liquid is an oxygen-containing liquid compound selected from the group consisting of ortho-cresol, meta-cresol, and 2,4-dimethylphenol.
Claim 14
Dependent Claim
25 words
The process as recited in claim 4, wherein said non-aqueous liquid is a liquid monohydric alcohol containing from about 1 to about 18 carbon atoms.
Claim 15
Dependent Claim
25 words
The process as recited in claim 4, wherein said non-aqueous liquid is a liquid polyhydric alcohol containing from about 2 to about 10 carbon atoms.
Claim 16
Dependent Claim
15 words
The process as recited in claim 4, wherein said non-aqueous liquid is liquid lubricating oil.
References Cited (Backward Citations)
US4104035A
Cited
US4282006A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-10-30 | 1988-04-30 | 1988-10-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-10-30 | 1992-04-30 | 1992-10-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-10-30 | 1996-04-30 | 1996-10-30 | $7700.00 | Window Closed / Lapsed |