USH1161H - Aqueous coal slurry - Google Patents
Aqueous coal slurry Download PDFInfo
- Publication number
- USH1161H USH1161H US07/428,682 US42868289A USH1161H US H1161 H USH1161 H US H1161H US 42868289 A US42868289 A US 42868289A US H1161 H USH1161 H US H1161H
- Authority
- US
- United States
- Prior art keywords
- dextrin
- coal
- weight
- concentration
- dispersant
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
- C10L1/326—Coal-water suspensions
Definitions
- the present invention is directed to a coal slurry and, more particularly, to an aqueous coal slurry containing dextrin as a dispersant.
- the cleaned coals When prepared as coal-water slurry fuel, the cleaned coals are often ground to a very fine particle size distribution to insure adequate combustion.
- the high surface area of cleaned, micronized coals can result in large demands for dispersants to achieve solids loadings suitable for specialized high-intensity combustion systems operating with coal-water slurry fuels. Because the dosages of the dispersant are generally greater than those required for coarser coal slurries for use in large industrial or utility boilers, the chemical composition of the dispersant becomes more important.
- alkali additions resulting from the use of an alkali-containing dispersant may have marked negative effects on ash characteristics when coal has been cleaned to low ash levels. Additionally, slurry sulfur values may also noticeably increase as a result of the use of a sulfur-containing dispersant.
- a principal object of the invention is the provision of an aqueous coal slurry containing a dispersant, which is of low-cost and which contains very low or no levels of sodium, potassium, sulfur and other contaminants.
- an object of the invention to provide an aqueous slurry containing coal and dextrin as a dispersant.
- Another object of the invention is to provide a method of preparing an aqueous coal slurry which includes the step of adding an effective amount of dextrin as a dispersant.
- An embodiment of the invention is an aqueous slurry containing coal and dextrin as a dispersant.
- the coal may be any one of several known varieties such as bituminous, anthracite, subbituminous, lignite and the like or mixtures thereof.
- the invention is particularly suitable for micronized coal in water but can be applied to carbonaceous particles or coarser coal particles.
- the dextrin is water-soluble and unbleached.
- the dextrin comprises a partially hydrolized starch (i.e., a polysaccharide) which is prepared by the heating or dry roasting of starch in the presence of an acid catalyst. Since dextrin is colloidal in property and describes a class of substances, it has no definite formula. Although STADEX® 120 and 126 dextrin manufactured by the Staley Manufacturing Company, Decatur, Illinois has been utilized, it is understood that the present invention is applicable to any type of dextrin.
- the concentration of coal in the aqueous slurry will range from about 44% to 61% by weight.
- the concentration of dextrin in the aqueous slurry will range from about 0.01% to 2.00% by weight.
- the slurry may also contain an additional dispersant such as ammonium naphthalene sulfonate, ammonium lignosulfonate, or an ammonium salt of a synthetic resin such as isobutylene/maleic anhydride.
- the concentration of the additional dispersant in the aqueous slurry is about 1.00% by weight for the ammonium naphthalene sulphate, and about 0.20% by weight for the ammonium lignosulfonate and the ammonium salt of a synthetic resin.
- the slurry may contain dextrin and a pH controlling reagent such as ammonium hydroxide.
- feedstocks representative of the types of coals which could be utilized in high-intensity combustion systems were prepared using heavy-media cleaning techniques. Following the heavy-media cleaning at a 1/2-inch particle top size, the coals were ground in a ball mill and then in a stirred ball mill at about 20 weight percent coal without any dispersing additives to achieve a particle top size of about 30 microns. Thereafter, the micronized coals were filtered to a moisture content suitable for the preparation of coal-water slurry fuel. The resulting product was a filter cake.
- ground filter cakes and coarser cleaned coals were utilized in different ways as exemplified in the following examples to determine the effectiveness of dextrin as a dispersant.
- Preground 30-micron top-size Indiana VII heavy-media float product coal (about 7.5 percent ash) was used for dextrin pretreatment tests.
- One slurry was prepared with a variable-speed mixer using the as-is, untreated (i.e., uncoated) filter cake.
- a second slurry was prepared using the pretreatment technique (dilution to 10 percent coal and high-speed mixing) without addition of dextrin (blank pretreatment).
- a third slurry was prepared from a filter cake which had been pretreated using 0.1 weight percent STADEX® 120 dextrin in a high-speed blender for 2 minutes at 10 percent coal concentration. The pretreated coal was filtered to a moisture content similar to the as-is, untreated filter cake prior to slurry preparation.
- the viscosity readings for the slurry containing 58.0 weight percent coal were obtained by grinding the coal with no dextrin present (as represented by the 0 in Table 4) and subsequently adding dextrin in incremental values after the removal of the coal from the grinder. Additionally, it is understood that the viscosity readings for the slurry containing 61.3 weight percent coal were obtained by grinding the coal in the presence of a 0.10 weight percent of dextrin (as represented by the 0.10 in Table 4) and, subsequently, adding dextrin in incremental values after removal of the coal from the grinder.
- a coal-water slurry containing dextrin and ammonium hydroxide as a pH controlling reagent was prepared using a minus 30-micron Indiana VII heavy-media product filter cake.
- the dextrin may be applied as a coal-surface pretreatment, as a co-additive with other conventional dispersants, or as a dispersant used only with a pH controlling reagent.
Abstract
An aqueous slurry containing coal and dextrin as a dispersant. The slurry, in addition to containing dextrin, may contain a conventional dispersant or, alternatively, a pH controlling reagent.
Description
The U.S. Government has rights in this invention pursuant to Contract No. DE-AC22-85PC80262 between the U.S. Department of Energy and AMAX Research & Development Center.
The present invention is directed to a coal slurry and, more particularly, to an aqueous coal slurry containing dextrin as a dispersant.
Many high-intensity combustion systems require that coal be cleaned to very low levels of ash to prevent excessive wear of high-temperature, high-speed components. For these applications, the cleaned coal must contain very low levels of alkali metals in order to prevent vaporization and subsequent deposition of corrosive inorganic constituents.
When prepared as coal-water slurry fuel, the cleaned coals are often ground to a very fine particle size distribution to insure adequate combustion. The high surface area of cleaned, micronized coals can result in large demands for dispersants to achieve solids loadings suitable for specialized high-intensity combustion systems operating with coal-water slurry fuels. Because the dosages of the dispersant are generally greater than those required for coarser coal slurries for use in large industrial or utility boilers, the chemical composition of the dispersant becomes more important.
A number of different dispersants for coal-water slurry production have been utilized in the industry. An example is U.S. Pat. No. 4,088,453 wherein ammonia is added to a coal-water slurry to improve pumpability. Many other dispersants incorporate the use of polyelectrolytes and sulfonates.
Upon combustion, alkali additions resulting from the use of an alkali-containing dispersant may have marked negative effects on ash characteristics when coal has been cleaned to low ash levels. Additionally, slurry sulfur values may also noticeably increase as a result of the use of a sulfur-containing dispersant.
A principal object of the invention is the provision of an aqueous coal slurry containing a dispersant, which is of low-cost and which contains very low or no levels of sodium, potassium, sulfur and other contaminants.
In connection with the foregoing object, it is an object of the invention to provide an aqueous slurry containing coal and dextrin as a dispersant.
Another object of the invention is to provide a method of preparing an aqueous coal slurry which includes the step of adding an effective amount of dextrin as a dispersant.
The invention consists of certain novel features and a combination of parts hereinafter fully described, and particularly pointed out in the appended claims, it being understood that various changes in the details may be made without departing from the spirit, or sacrificing any of the advantages of the present invention.
An embodiment of the invention is an aqueous slurry containing coal and dextrin as a dispersant.
According to the invention, the coal may be any one of several known varieties such as bituminous, anthracite, subbituminous, lignite and the like or mixtures thereof. The invention is particularly suitable for micronized coal in water but can be applied to carbonaceous particles or coarser coal particles.
According to the invention, the dextrin is water-soluble and unbleached. The dextrin comprises a partially hydrolized starch (i.e., a polysaccharide) which is prepared by the heating or dry roasting of starch in the presence of an acid catalyst. Since dextrin is colloidal in property and describes a class of substances, it has no definite formula. Although STADEX® 120 and 126 dextrin manufactured by the Staley Manufacturing Company, Decatur, Illinois has been utilized, it is understood that the present invention is applicable to any type of dextrin.
The concentration of coal in the aqueous slurry will range from about 44% to 61% by weight. The concentration of dextrin in the aqueous slurry will range from about 0.01% to 2.00% by weight.
In addition to the dextrin, the slurry may also contain an additional dispersant such as ammonium naphthalene sulfonate, ammonium lignosulfonate, or an ammonium salt of a synthetic resin such as isobutylene/maleic anhydride. The concentration of the additional dispersant in the aqueous slurry is about 1.00% by weight for the ammonium naphthalene sulphate, and about 0.20% by weight for the ammonium lignosulfonate and the ammonium salt of a synthetic resin.
Alternatively, the slurry may contain dextrin and a pH controlling reagent such as ammonium hydroxide.
It is understood that the optimum concentration levels for the dextrin, conventional dispersants, or the pH modifier additive levels can be determined for each specific application on the basis of coal type, desired slurry properties, and economics by one skilled in the art.
For a fuller understanding of the nature and advantages of the present invention, reference is made to the following examples wherein the effectiveness of dextrin is shown when used as: 1) a coal surface pretreatment, 2) a co-additive with the conventional dispersants described above, and 3) a dispersant used only in combination with the pH controlling reagent. These examples are given merely to illustrate the invention and are not to be construed in a limiting sense.
In each of the examples to follow, feedstocks representative of the types of coals which could be utilized in high-intensity combustion systems were prepared using heavy-media cleaning techniques. Following the heavy-media cleaning at a 1/2-inch particle top size, the coals were ground in a ball mill and then in a stirred ball mill at about 20 weight percent coal without any dispersing additives to achieve a particle top size of about 30 microns. Thereafter, the micronized coals were filtered to a moisture content suitable for the preparation of coal-water slurry fuel. The resulting product was a filter cake.
The ground filter cakes and coarser cleaned coals were utilized in different ways as exemplified in the following examples to determine the effectiveness of dextrin as a dispersant.
Preground 30-micron top-size Indiana VII heavy-media float product coal (about 7.5 percent ash) was used for dextrin pretreatment tests. Three different slurries were prepared from treated and untreated coal filter cakes using a 1.0 percent dosage of A-23 ammonium naphthalene sulfonate dispersant manufactured by the Diamond Shamrock Corporation, Morristown, N.J.
One slurry was prepared with a variable-speed mixer using the as-is, untreated (i.e., uncoated) filter cake. A second slurry was prepared using the pretreatment technique (dilution to 10 percent coal and high-speed mixing) without addition of dextrin (blank pretreatment). A third slurry was prepared from a filter cake which had been pretreated using 0.1 weight percent STADEX® 120 dextrin in a high-speed blender for 2 minutes at 10 percent coal concentration. The pretreated coal was filtered to a moisture content similar to the as-is, untreated filter cake prior to slurry preparation.
The results are summarized in Table 1 which shows that the weight percent of coal at a slurry viscosity of 500 cp increased after scrubbing the coal surfaces in deionized water (blank pretreatment), and that the weight percent of coal increased further from the addition of dextrin. During testing, the viscosity of the slurry was kept constant by the removal of water in response to the addition of dextrin.
TABLE 1
______________________________________
Preparation of a Coal-Water Slurry from Filter Cakes Using
Dextrin Pretreatment and A-23 Ammonium Naphthalene Sulfon-
ate Dispersant. (Indiana VII Heavy-Media Float Product Coal)
Dextrin Weight % Coal at
Pretreatment Dispersant
500 cp Viscosity
______________________________________
none 1.0% ˜41
0% STADEX ® 120
1.0% *46.5
(blank)
0.1% STADEX ® 120
1.0% 47.5
______________________________________
*Weight percent of coal after scrubbing the coal surface in deionized
water.
Tests similar to those described above using a Kentucky 4a physically-cleaned coal feedstock (4.5 percent ash) and STADEX® 126 dextrin. The results are summarized in Table 2 which shows that pretreatment with 0.1 weight percent of dextrin helped to increase solids loading from 53.3 to 54.7 percent coal when measured at a comparable slurry viscosity of 200 cp.
TABLE 2
______________________________________
Preparation of a Coal-Water Slurry from Filter Cakes Using
Dextrin Pretreatment and A-23 Ammonium Naphthalene Sulfon-
ate Dispersant. (Kentucky 4a Heavy-Media Float Product coal)
Dextrin Weight % Coal at
Pretreatment Dispersant
200 cp Viscosity
______________________________________
none 1.0% 53.4
0% STADEX ® 126
1.0% *53.3
(blank)
0.1% STADEX ® 126
1.0% 54.7
______________________________________
*Weight percent of coal after scrubbing the coal surface in deionized
water.
An Elkhorn seam heavy-media float product coal (about 1 percent ash) was used for these tests. Minus 1/8-inch coal was ground in a laboratory rod mill for 90 minutes in the presence of deionized water, conventional dispersants, and, in some cases, dextrin.
The results are summarized in Table 3 which shows that the STADEX® 126 dextrin enhanced the coal-water slurry dispersion characteristics as measured by the greater production of fines during grinding (i.e., greater % of coal particles less than 37 microns) without sacrificing the weight percent of coal in the slurry or the viscosity of the slurry.
TABLE 3
______________________________________
Preparation of a Coal-Water Slurry Using Dextrin and Conven-
tional Dispersants. (Elkhorn Heavy-Media Float Product Coal)
*Additives, Wt % Product Wt % Coal In
STADEX ®
**D- **Tamol Particle Size, %
Slurry at
126 319-2 165 <37 microns
500 cp viscosity
______________________________________
0 0.20 -- 81.5 59.4
1.0 0.20 -- 92.2 59.6
0 -- 0.20 86.3 60.4
1.0 -- 0.20 90.8 60.2
______________________________________
*Additive dosages are based on active reagent and dry coal weight.
**D319-2 is an ammonium lignosulfonate manufactured by ReedLignin,
Greenwich, Connecticut. Tamol 165 is an ammonium salt of a synthetic
resin, possibly isobutylene/maleic anhydride, manufactured by Rohm and
Haas, Philadelphia, Pennsylvania.
Further tests revealed that the addition of dextrin after grinding reduced the viscosity of the resulting aqueous slurry (i.e., a desirable feature for the efficient transportation of the slurry). The results are summarized in Table 4 which shows that the incremental addition of dextrin to a slurry prepared using 0.20 weight percent of Tamol 165 dispersant resulted in significant reduction in viscosity.
It is understood that the viscosity readings for the slurry containing 58.0 weight percent coal were obtained by grinding the coal with no dextrin present (as represented by the 0 in Table 4) and subsequently adding dextrin in incremental values after the removal of the coal from the grinder. Additionally, it is understood that the viscosity readings for the slurry containing 61.3 weight percent coal were obtained by grinding the coal in the presence of a 0.10 weight percent of dextrin (as represented by the 0.10 in Table 4) and, subsequently, adding dextrin in incremental values after removal of the coal from the grinder.
TABLE 4
______________________________________
Effect of STADEX ® 126 Dextrin Concentration on
Elkhorn No. 3 Coal-Water Slurry Viscosity.
Brookfield Viscometer
Additive Concentration
Scale-Reading (T-B
Wt % Measurement Spindle)
Coal Tamol 165 STADEX ® 126
50 rpm 100 rpm
______________________________________
58.0 0.20 0 (as-ground)
86 >95
58.0 0.20 0.01 81 >95
58.0 0.20 0.06 57 91
58.0 0.20 0.16 45 59
58.0 0.20 0.36 15 34
58.0 0.20 0.86 7.5 19
58.0 0.20 1.11 4.8 16
58.0 0.20 1.36 4.8 14
61.3 0.20 0.10 (as-ground)
>95 >95
61.3 0.20 0.11 >95 >95
61.3 0.20 0.16 >95 >95
61.3 0.20 0.26 75 >95
61.3 0.20 0.46 20 55
61.3 0.20 0.96 11 36
61.3 0.20 1.21 1.5 36
61.3 0.20 1.46 1.5 36
______________________________________
A coal-water slurry containing dextrin and ammonium hydroxide as a pH controlling reagent was prepared using a minus 30-micron Indiana VII heavy-media product filter cake.
The results are summarized in Table 5 which compares the effects of using no dextrin, ammonium hydroxide only, and dextrin with ammonium hydroxide. As shown therein, significant improvement in weight percent of solids loading at a slurry viscosity of 100 cp was achieved using dextrin in addition to a pH modifier.
As shown in Table 6, a slurry containing dextrin and ammonium hydroxide exhibited decreasing viscosity with increasing temperature, a desirable feature for many high-intensity combustion applications where slurry preheating is required. Measurements were made with a Fann® Model 50C viscometer using a nitrogen gas overpressure to prevent moisture loss from the samples.
TABLE 5
______________________________________
Preparation of a Coal-Water Slurry Using
Dextrin and Ammonium Hydroxide.
(Indiana VII Heavy-Media Float Product Coal)
Weight % Coal at
Additive pH 100 cp Viscosity
______________________________________
none 6 38
ammonium hydroxide
7 41.8
ammonium hydroxide +
7 44.8
2% STADEX ® 126
______________________________________
TABLE 6
______________________________________
Effect of Temperature on Slurry Viscosity
(Indiana VII Heavy-Media Float Product
Coat Containing Dextrin and Ammonium Hydroxide)
Temperature, °F.
Viscosity, cp at 500/sec shear rate
______________________________________
90 492
124 344
213 340
302 296
______________________________________
What has been described therefore is an improvement in the dispersion of a coal-water slurry by the utilization of dextrin The dextrin may be applied as a coal-surface pretreatment, as a co-additive with other conventional dispersants, or as a dispersant used only with a pH controlling reagent.
Claims (7)
1. An aqueous slurry containing coal particles having a partial top size of about 30 microns and dextrin as a dispersant at a concentration between about 0.01% and about 2.00% by weight, and an additional dispersant selected from the group consisting of ammonium naphthalene sulfonate at a concentration of about 1.00% by weight, ammonium lignosulfonate at a concentration of about 0.20% by weight, or an ammonium salt of a synthetic resin at a concentration of about 0.20% by weight.
2. An aqueous slurry containing coal particles having a particle top size of about 30 microns, dextrin at a concentration of about 2.00% by weight, and a pH controlling reagent in an amount effective to maintain a pH of about 7.
3. A method of preparing an aqueous coal slurry containing coal particles having a particle top size of about 37 microns, dextrin, and an additional dispersant including the step of adding said dextrin and said additional dispersant during the grinding of the coal, said dextrin being present at a concentration of about 1.00% by weight and said additional dispersant comprising an ammonium lignosulfonate or an ammonium salt of a synthetic resin present at a concentration of about 0.20% by weight.
4. A method of preparing an aqueous slurry containing coal particles having a particle top size of about 30 microns, dextrin, and an additional dispersant including the step of adding said dextrin and said additional dispersant to a coal filter cake prior to said coal being introduced to a said slurry, said dextrin and said additional dispersant being added in an amount effective to disperse the coal in the slurry.
5. The method of claim 4, wherein said additional dispersant comprises ammonium naphthalene sulfonate and is present at a concentration of about 1.00% by weight.
6. The method of claim 3, further including the step of adding an additional amount of dextrin after the grinding of said coal.
7. The method of claim 6, wherein said additional amount of dextrin is added such that the concentration of said dextrin is between about 0.10% and about 1.46% by weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/428,682 USH1161H (en) | 1989-10-30 | 1989-10-30 | Aqueous coal slurry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/428,682 USH1161H (en) | 1989-10-30 | 1989-10-30 | Aqueous coal slurry |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USH1161H true USH1161H (en) | 1993-04-06 |
Family
ID=23699929
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/428,682 Abandoned USH1161H (en) | 1989-10-30 | 1989-10-30 | Aqueous coal slurry |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | USH1161H (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100202245A1 (en) * | 2006-08-14 | 2010-08-12 | Eastman Chemical Company | Agitation system and method for measuring settling rate of solids from a suspension |
Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4088453A (en) | 1976-06-24 | 1978-05-09 | Texaco Inc. | Production of solid fuel-water slurries |
| US4217109A (en) | 1977-05-31 | 1980-08-12 | Ab Scaniainventor | Composition comprising a pulverized purified substance, water and a dispersing agent, and a method for preparing the composition |
| US4261701A (en) | 1980-01-09 | 1981-04-14 | Gulf Research & Development Company | Uniform coal suspensions and process for preparing same |
| US4302212A (en) | 1979-07-26 | 1981-11-24 | Kao Soap Company, Limited | Dispersing agents for an aqueous slurry of coal powder |
| US4375358A (en) | 1980-09-02 | 1983-03-01 | Conoco Inc. | Fuel slurries of solid carbonaceous material in water |
| US4436528A (en) | 1982-09-17 | 1984-03-13 | Diamond Shamrock Chemicals Company | Aqueous slurries of carbonaceous materials |
| US4455149A (en) | 1981-04-16 | 1984-06-19 | Maruzen Oil Co., Ltd. | Process for the production of fuel compositions |
| US4472170A (en) | 1982-12-27 | 1984-09-18 | The Procter & Gamble Company | Coal-water slurry compositions |
| US4500041A (en) | 1981-12-03 | 1985-02-19 | Lion Corporation | Process for producing high-concentration slurry of coal |
| US4552568A (en) | 1982-07-24 | 1985-11-12 | Nippon Oil And Fats Co., Ltd. | Method for preparing coal-water slurry |
| US4597770A (en) | 1984-12-24 | 1986-07-01 | The Procter & Gamble Company | Coal-water slurry compositions |
| US4650496A (en) | 1978-11-02 | 1987-03-17 | Alfred University Research Foundation, Inc. | Process for making a carbonaceous slurry |
| US4652271A (en) | 1985-04-12 | 1987-03-24 | Henkel Kommanditgesellschaft Auf Aktien | Coal suspension flowability improvers |
| US4713086A (en) | 1984-03-02 | 1987-12-15 | Amax Inc. | Oil-compatible coal/water mixtures |
| US4744797A (en) | 1984-04-21 | 1988-05-17 | Yoshinari Shimada | Mixed fuel of coal powder or the like and heavy oil |
| US4770352A (en) | 1986-04-17 | 1988-09-13 | Babcock-Hitachi Kabushiki Kaisha | Coal-water slurry producing system |
-
1989
- 1989-10-30 US US07/428,682 patent/USH1161H/en not_active Abandoned
Patent Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4088453A (en) | 1976-06-24 | 1978-05-09 | Texaco Inc. | Production of solid fuel-water slurries |
| US4217109A (en) | 1977-05-31 | 1980-08-12 | Ab Scaniainventor | Composition comprising a pulverized purified substance, water and a dispersing agent, and a method for preparing the composition |
| US4650496A (en) | 1978-11-02 | 1987-03-17 | Alfred University Research Foundation, Inc. | Process for making a carbonaceous slurry |
| US4302212A (en) | 1979-07-26 | 1981-11-24 | Kao Soap Company, Limited | Dispersing agents for an aqueous slurry of coal powder |
| US4261701A (en) | 1980-01-09 | 1981-04-14 | Gulf Research & Development Company | Uniform coal suspensions and process for preparing same |
| US4375358A (en) | 1980-09-02 | 1983-03-01 | Conoco Inc. | Fuel slurries of solid carbonaceous material in water |
| US4455149A (en) | 1981-04-16 | 1984-06-19 | Maruzen Oil Co., Ltd. | Process for the production of fuel compositions |
| US4500041A (en) | 1981-12-03 | 1985-02-19 | Lion Corporation | Process for producing high-concentration slurry of coal |
| US4552568A (en) | 1982-07-24 | 1985-11-12 | Nippon Oil And Fats Co., Ltd. | Method for preparing coal-water slurry |
| US4436528A (en) | 1982-09-17 | 1984-03-13 | Diamond Shamrock Chemicals Company | Aqueous slurries of carbonaceous materials |
| US4472170A (en) | 1982-12-27 | 1984-09-18 | The Procter & Gamble Company | Coal-water slurry compositions |
| US4713086A (en) | 1984-03-02 | 1987-12-15 | Amax Inc. | Oil-compatible coal/water mixtures |
| US4744797A (en) | 1984-04-21 | 1988-05-17 | Yoshinari Shimada | Mixed fuel of coal powder or the like and heavy oil |
| US4597770A (en) | 1984-12-24 | 1986-07-01 | The Procter & Gamble Company | Coal-water slurry compositions |
| US4652271A (en) | 1985-04-12 | 1987-03-24 | Henkel Kommanditgesellschaft Auf Aktien | Coal suspension flowability improvers |
| US4770352A (en) | 1986-04-17 | 1988-09-13 | Babcock-Hitachi Kabushiki Kaisha | Coal-water slurry producing system |
Non-Patent Citations (3)
| Title |
|---|
| Berggren and Swanson, "Development of Dispersing Additives for Ultra-Clean Coal-Water Slurry Fuels", Twelfth International Conference on Slurry Technology, 1987. |
| Berggren and Swanson, Final Report, Contract No. DE-AC22-85PC80262. |
| Staley Industrial Products, Technical Data. |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100202245A1 (en) * | 2006-08-14 | 2010-08-12 | Eastman Chemical Company | Agitation system and method for measuring settling rate of solids from a suspension |
| US8313229B2 (en) | 2006-08-14 | 2012-11-20 | Eastman Chemical Company | Agitation system and method for measuring settling rate of solids from a suspension |
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