Method of producing coal water suspension

专利摘要:
A coal - water slurry at high concentration which has a low viscosity and favorable flowing property is prepared by using a surface active substance prepared by sulfonating and oxidizing at least one of the starting materials selected from distilled petroleum oils, petroleum pitches, asphalts, distilled coal oils, coal pitches or coals, applying condensation as required and then neutralizing the thus obtained product with alkalis.
公开号:SU1538901A3
申请号:SU864027907
申请日:1986-07-22
公开日:1990-01-23
发明作者:Морита Язаемон；Окада Синити；Инагаки Кацуо；Накамура Есинобу；Гото Тадао；Фудзикура Исао
申请人:Фудзи Ойл Ко, Лтд (Фирма)；Тохо Кемикал Индастри Ко, Лтд (Фирма)；
IPC主号:

专利说明:

i
(21) 4027907 / 23-04
(22) 07.22.86
(31) 163234/85
(32) 07.23.85
(33) JP
(46) 01/23/90. Bksh. Number 3
(71) Fuji Oil Co., Ltd. and Toho-Chemikal Industry Co., Ltd. (JP)
(72) Yazaemon Morita, Shinichi Okada, Katsuo Inagaki, Yoshinobu Nakamura, Tadao Goto and Isao Fujikura (JP)
(53) 662.65 (088.8)
(56) Patent ША № 4364742, кл. 44-51, 1982.
US patent number 4465495, CL.44-51, 1984.
(54) METHOD FOR OBTAINING A WATER-ANGLE SUSPENSION
(57) The invention relates to coal chemistry, in particular the preparation of a coal-water slurry suitable for transportation through pipelines. The goal is to reduce the viscosity of the slurry. The process is conducted by mixing fine coal, water and dispersant. As the latter, the product is used for sulfonation of petroleum or coal bitumen, or both basic coal, or petroleum asphalt, or asphalt after solvent deasphalting, or a mixture of petroleum and coal bitumen having a mol. 300-4520 and the ratio of hydrogen to carbon, 0.65-1.47. The resulting product is then oxidized with nitric oxide and neutralized with alkali to obtain a product containing 0.5-7.9 mg equiv / g of sulfonyl groups and 3.6-15 mg eq / g of acid groups. It is better to carry out the sulfonation after grinding the source material with sulfuric acid in tetrachloroethane, tetrachlorethylene or perchlorethylene. After dispersion, the resulting mixture is homogenized. These conditions ensure the concentration of coal in the suspension (up to 71%), its good flowability (viscosity up to 630) and stability. 2 hp f-ly, 5 tab.
i
ABOUT)
ta
with
00 WITH
The invention relates to a method for preparing a surfactant for producing a highly concentrated coal-water slurry having a low viscosity and good flowability, as well as satisfactory stability, and can be used as an energy fuel.
The purpose of the invention is to reduce the viscosity of the slurry.
Example 1.1. Synthesis of surfactant (surfactant-dispersant) 1 according to the invention.
A mixture of different types of crude oil, including Hafd crude oil, and Iranian heavy crude oil, in a 1: 1 volume ratio, is treated at a reduced pressure of 60 mm Hg. at 340 ° C to obtain a petroleum residue having a specific weight of 1.022 g / cm (at 25 ° C), melting point 44 ° C, a residual carbon content of 19.5 wt.%, which is then treated at a pressure of 2 kg / cm and temperature using superheated steam at.

cm
600 ° C for 2 hours to obtain oil bitumens with a melting point of 180 ° C, a volatile content of 40% by weight, ash of 0.2% by weight, and an H / C atomic ratio of 0.8. These petroleum bitumens are called source material A and have a mol.m. 1100. Bitumens are ground into powder with a particle size of less than 100 mesh, 1 wt.h. the powder is placed in a glass autoclave, 5 wt.h is added. tetrachloroethane, then the mixture of bitumen and solvent is stirred with a mixer, rotating at 500 rpm, 2.0 wt.h. preliminarily evaporated by heating anhydrous sulfuric acid is introduced to carry out the sulfonation reaction at 50 ° C for 60 minutes under atmospheric pressure. After that, the temperature is increased to 120 ° C, 5 math is added. 50% nitric acid and oxidation are carried out for 2 hours. Then, after filtration, washing with water and drying the reaction product, a part of it is taken to determine the content of sulfonyl groups and the total content of acidic groups by known methods. The reaction product contains 5.7 mg eq./g of sulfonyl groups of 13.1 mg eq./g of acidic groups. After neutralizing the product with caustic soda to a pH of 1% aqueous solution equal to 8.0, the product is dried and ground to obtain a surfactant-1 by the proposed method in the form of a black powder (Table 1).
Ii. Synthesis of surfactant 2 - 6.9 and 10 according to the invention.
Surfactants 2-6.9 and 10 are synthesized by the same procedures as surfactant-1 using the same petroleum bitumen (starting material A) as the starting material, anhydrous sulfuric acid as the sulphating agent, tetrachloroethane or perchloroethane in as a solvent; and sulfuric acid; or nitric acid as an oxidizing agent.
Synthesis of surfactant-9. Petroleum pitches (raw material A) are ground to a powder with a particle size less than 100 IU 1 wt. the powder is placed in a glass autoclave, where it is dispersed by adding 5 wt. tetrachloro ethylene with simultaneous mixing at a speed of 500 rpm. Then, in order to carry out the sulfonation reaction at 50 dC for 1 h, the introduction
Q p 5 5
50 55
0
45
1.0 ma.ch. gasified anhydrous sulfuric acid.
After that, the temperature is raised to 120 ° C and oxidized by the introduction of 4.0 May. 50% nitric acid for 2 hours. After filtration, washing with water and drying the reaction product, the sulfo and total acid groups are determined in the usual way, resulting in a sulfo group content of 4.6 mEq. / g and 9.8 mgh eq / g of all acid groups. The product is neutralized with sodium hydroxide in order to bring the pH of the 1% aqueous solution to 8.0, followed by drying and grinding the product to obtain the surfactant 9 (surfactant-9) in the form of a black powder.
The properties of surfactant-1 and surfactant 2-6.9 and 10 are also given in table. one "
III. Synthesis of surfactant-7 and surfactant-8 according to the invention.
Surfactant-7 and surfactant-8 are synthesized using the same petroleum bitumen (starting material A) as for surfactant 1 using 98% sulfuric acid or 60% oleum as the sulfidizing agent. The sulfonation is carried out without the use of a chlorine-containing hydrocarbon solvent, but under the conditions shown in Table. 1, in which the bitumens are premixed with concentrated sulfuric acid or oleum in a mortar, then placed in a glass autoclave and stirred while rotating the agitator at a frequency of 100 rpm at 40 ° C for 60 minutes. Then 1 mah. the resulting sulfonation product is taken from a glass autoclave and oxidized under the conditions shown in Table 2. one.
IV. Synthesis of surfactant-11 - surfactant-13 according to the invention.
North American high coking coal is dry distilled and the distilled coal resins are cracked under the same conditions as the raw material for surfactant-1. After that, the surfactant-11 is synthesized by the surfactant-13 as well as the surfactant-1 (Table 1), while the resulting coal bitumen (raw material B) has a melting point of 180 ° C, the content of volatile components is 37.5%, atomic ratio H / C - 0.79 and mol. 360 m.
5153
V. Synthesis of surfactant-14, surfactant-15 according to the invention.
Desalted bituminous coal of the North American region with a moisture content of 2.8 wt.%, Mol.m. 3000, ash content of 0.9 wt.%, Volatile substances of 14.5 wt.%, N / C of 0.65, carbon content of 63.0 wt.%, Used as a starting material (starting material C). In this case, surfactant-14 and surfactant-15 are synthesized in the same way as surfactant-1 (Table 1).
VI. Synthesis of surfactant-16 - surfactant-18 according to the invention.
A mixture of different types of crude oil, including crude from the South American Bacakero field, the Middle East Hafji field, Iranian heavy oil and heavy oil Istumus in a volume ratio of 4: 2: 1: 1,
under reduced pressure of 70 mm Hg. at 335 ° C. Surfactants 16-18 are synthesized from asphalt obtained by distillation and having a specific weight at 25 ° С 1,0115 g / mb, melting point 38.5 С, residual carbon content 16.9 wt.%, Atomic ratio Н / С 1.45 and mol.m. 1050. After dissolving asphalt at 50 ° C for 5 minutes in tetrachloroethane, surfactants are synthesized as surfactant-1 (Table 1).
VII. Synthesis of surfactant-19 - surfactant-22 according to the invention.
The surfactant-19 -surfactant-22 is obtained from a bitumen obtained by mixing the starting material for the surfactant-1 and the starting material for the surfactant-11 - the surfactant-13 in a 1: 1 weight ratio (the starting material E which has a melting point of 148 C, volatile substances: 39.1 wt.% 7 atomic ratio H / C 0.8 and mol.m. 1100 under the conditions shown in Table 1.
VIII. Synthesis of surfactant-23 according to the invention.
The mixture of crude oil of the Baccacero, Arabian light crude and Arabian heavy crude in a volume ratio of 5: 2: 1 is distilled under the same conditions as for the raw material A during the synthesis of surfactant-1 and a heavy residue is obtained. at 25 ° C, equal to 1.0310 g / cm3, melting point 47.5 C and residual carbon content of 21.4 wt.%, which is subjected to cracking, as well as the starting material A and the resulting oil
01

0
five
five
50
five
0
The tar bitumen (starting material D) with a melting point of 220 ° C, a volatile content of 32% by weight, ash of 0.2% by weight and an H / C atomic ratio of 0.68 is used as the starting material. The bitumen is ground to a powder with a particle size of less than 100 mesh and one part of this powder is placed in an autoclave made of glass, where it is dissolved and dispersed in 10 parts by weight. tetrachlorethylene at 110 ° C for 30 min with stirring at a frequency of 500 rpm. The mixture is then cooled to 15 ° C, after which 1.5 parts by weight are added to it. gasified anhydrous sulfuric acid to carry out the sulfonation reaction for 1 hour.
After that, the temperature is raised to 130 ° C and oxidized by the addition of 2.0 parts by weight. gasified nitrogen mixture for 2 hours. After filtration, washing with water and drying, the amount of sulfonyl groups and the total amount of acid groups of the obtained reaction product, which contains 5.0 mg eq / g of sulfonyl groups and 11.6 mg eq / g, are measured. sour groups. The product is neutralized with caustic soda to a pH of 1% solution, equal to 8.0, after which it is dried and ground to obtain a black powder.
Ix. Synthesis of surfactant-24 according to the invention.
Sweet and reduced gas oils and heavy gas oils in a 4: 1 volume ratio are subjected to catalytic cracking (reaction temperature of 530 ° C with a zeolite catalyst) to obtain heavy residues with a specific gravity (15/4 ° C) of 1.0971 g / cm , boiling point from 200 to 538 ° С, atomic ratio Н / С 0.96 and average mol.m. 300 (source material D). 1 ma.ch. the starting material is placed in a glass autoclave, which is fed 5 mas. tetrachloroethane and 1 ma.ch. gasified anhydrous sulfuric acid at 15 ° C and with stirring at a frequency of LOO rpm to carry out the sulfonation for 1 hour. Then the temperature is raised to 120 ° C and 2 wt. hours added. nitrogen dioxide gas to oxidize for 2 hours.
After filtering off the reaction product, the content of sulfonyl groups in it and the total amount of 7153890 are measured.
in acidic groups, which is equal to 4.2 mg hekv / g and 6.8 mg. equiv / g, respectively. Thereafter, the reaction product is neutralized with caustic soda so as to obtain a pH of 1% aqueous solution equal to 8, which is then dehydrated, crushed to obtain a black powder.
X. Synthesis of surfactant-25 according to inventive {genius.
1 h of thermally cracked oils with a boiling range of 400-538 ° C are used as the starting material.
a specific weight (15/4 C), equal to 9810 g / cm, atomic ratio
15
20
25
thirty
/ With 1.47 and the average mol.m. 500 (source material H). 1 ma.ch. This starting material is placed in a glass vault along with 5 parts by weight. tetrachloroethane and 1 ma.ch. gasified sulfuric acid and sulphate for 1 hour at 30 ° C with stirring at a frequency of 500 rpm. The temperature is then increased to 1209 ° C and oxidized by the introduction of gaseous nitrogen dioxide in the amount of 1 wt. Hours. within 1 h. Reaction product from -. The contents of the sulfonyl groups and the total content of acidic groups, which turned out to be 3.9 mg-eq / g and 7.1 mg csv / g, are determined and determined. The reaction product is neutralized with sodium hydroxide to obtain a pH of a 1% aqueous solution of 8.0, after which it is dehydrated and ground to 35 to obtain a black powder. Xi. Synthesis of IIAB-26 according to the invention.
To effect condensation with formaldehyde, non-neutralized surfactant-9 is treated as follows.
First neutralized with sodium hydroxide to bring the pH to 8.0 in 2 parts by weight. distilled water. Then 3 math are introduced into the solution. cation exchange resin with simultaneous mixing in order to bring the pH of the aqueous solution to 4.0 by replacing the cation exchange resin with an acidic type resin.
After filtering the ion exchange resin from the aqueous solution, an acidic aqueous solution of surfactant-9 is obtained, which is placed in an amount of 1 wt. in a glass- $ 5 lnny autoclave and dispersed in 2 m.ch. purified water. Then, 0.3 mph was introduced into the autoclave. 96% sulfuric acid and 0.3 wt. formal 40
45
50
five
0
five
thirty
35
$ 5
40
45
50
eight
a guide having a temperature of 37 ° C. The process is carried out at 90 ° C for 2 hours with stirring at a frequency of 500 rpm, and the mixture is kept for 7 hours to carry out a condensation reaction.
After completion of the reaction, the reaction product is washed with water and neutralized with caustic soda so as to bring the pH of the 1% aqueous solution to 8.0. After that, the product is dried and ground to obtain a surfactant-26 in the form of a black powder. The viscosities of the surfactant-26 and surfactant-9 thus obtained are equal to OJ25 (surfactant-9) and 0.510 HPAW-26), which indicates that formaldehyde condensation has passed.
Xii. Synthesis of surfactant-27 - surfactant-30 according to the invention.
Surfactant-27 - Surfactant-30 is of the formaldehyde-condensation type and is synthesized in the same way as surfactant-26.
The reaction temperature and the time of formaldehyde condensation are exactly the same with surfactant-26.
The research results are shown in Table. 2
Data on the content of sulfo - and acid groups in the surfactant-26 - surfactant-30 are presented in Table. 3
Xiv. Synthesis of surfactant-31 according to the invention.
Petroleum pitches (raw material A) are ground to a powder with a particle size of less than 200 mesh, more than 90% of them are passed through a ball mill and placed in a glass autoclave for 1 hour, where they are dissolved and dispersed by adding 3 wt. tetrachlorethylene while stirring at 500 rpm. Thereafter, to perform the sulfonation reaction, 0.5 wt.h. liquid anhydrous sulfuric acid.
After that, the temperature is raised to 100 ° C and oxidized by the introduction of 2.0 parts by weight. 61% nitric acid for 2 hours. After filtration, washing with water and drying the reaction product, the sulfonic acid groups were determined, which gave the following results: 1.2 mg eq / g of sulfo groups and 4.8 mg hectv / g of all acid groups. The product is neutralized with sodium hydroxide with the addition of a pH of 1% aqueous solution to 8.0 followed by.
drying and grinding in the form of a black powder.
Xv. Synthesis of surfactant-32 according to the invention.
The bottoms (asphalt, bitumen) obtained by distillation under reduced pressure from a mixture of crude oils, consisting of crude oil from the Khafji field and other middle-eastern crude oils, and characterized by a specific weight (20/4 ° С) equal to 1.0310 g / cm, softening temperature 46 ° С, atomic ratio Н / С, equal to 1.43 and average mol.m. 1150, deasphalted by pentane. Asphalts, deasphalted by pentane (raw material P), have a specific weight (20/4 ° С) of 1.1504 g / cm3, Н / С 1.16 and mol.m. 4520. 1 mac. the deasphalted material P is placed in a glass autoclave, where it is dissolved and dispersed by adding 5 parts by weight. tetrachlorethylene with simultaneous repro mixing at a rotation speed of 500 rpm. After that, 0.1 m / h was introduced for sulphonation at room temperature for 30 minutes. gasified anhydrous sulfuric acid.
After that, the temperature is raised to 120 ° C and oxidized by the introduction of 3.0 parts by weight. liquefied shg over
1 h, and then incubated for 2 h. After filtration, water washing and drying of the reaction product, the sulfonic acid groups are determined, which gave the following results: 0.5 mg hakev / g of sulfo groups and 3.6 mg equiv / g of acid groups. The product is subjected to neutralization with sodium hydroxide to bring the pH of a 1% aqueous solution to 8.0, followed by drying and grinding to obtain a brown powder.
Xiii. Preparation of coal-water slurry according to the invention.
Coal Wallara containing 2.8 wt.% Moisture, 13.5 wt.% Ash, 24.6 wt.% Volatile components and 56.5 wt.% Carbon, crushed in a finger mill, and then attrition in a disk mill in the form of 50% WUS for 30 minutes to obtain coal particles with a size of 82% grains passing through a 200 mesh screen.
The coal-water slurry is then heated and the water is evaporated to obtain 80% by weight of a solid mixture.

15
20
25
thirty
20 ° С
ten
ponenta. To each 100 g of product, 0.4 g of surfactant-1 - surfactant-30 and water are added so that the coal concentration is 68 wt. Parts, after which the mixture is stirred for 10 minutes in a mixer to obtain highly concentrated suspensions. If, at such a concentration, the fluidity does not reach IQ s, water is added until the desired fluidity is reached.
The results of viscosity measurements are given in table. four.
Viscosity values were obtained with rotor No. 3 at 12 rpm.
The water suspension (samples 3,6,7,10,12,14,15,17,18,20,22,24,26 and 30) was stored at room temperature for 6 months in 100 ml bottles and then checked the presence of sediment at the bottom of the bottles by the introduction of a glass rod. No sediment was detected in any of the samples.
The comparative surfactants used in this test are also added in an amount of 0.4 g per 100 g of coal-water slurry.
Comparative surfactant-1: sodium sulfate poly (10) oxyethylene laurie ether.
Comparative Surfactant-2: poly (20) hydroxyethylene nonylphenyl ether.
Comparative Surfactant-3: poly (15) hydroxy ethylene poly (15) hydroxy propylene sten-35-nyl ether.
Comparative surfactant-4. Arabian light crude oils are subjected to distillation at atmospheric pressure to obtain distilled Fractions with a boiling interval of 230-330 ° C, specific gravity (15/4 ° C) 0.8435 g / cm, atomic ratio H / C 1.79 and average mol.m. 180, 1 ma.ch. the starting material is placed in a glass autoclave 45 and dissolved in 2 parts of tetracholoethene, after which gasified anhydrous sulfuric acid is introduced in an amount of 0.3 wt. at 20 ° C and with stirring at a frequency of 500 rpm for 50 hours of sulfonation. After that, the temperature is raised to 120 ° C and oxidized by adding 2 mash. gaseous nitrogen dioxide for 3 hours
55 Then, after filtering out tetrachlorethylene, in which unreacted oils are dissolved, and the resinous reaction product, the content of groups and acid groups is determined,
eleven
which is 2.1 mg eq / g and 5.1 mgx j / eq / g, respectively.
The resulting product is neutralized with caustic soda so that its 1% aqueous solution has a pH of 8.0 and then concentrated to 50% concentration to obtain a comparative surfactant-4 in the form of light yellow (liquid.
Comparative IIAB-5. Ligroin fraction of a mixture of Middle Eastern raw oil of various deposits with an interpall boiling point of 80-160 ° С hydrogenation153890112
wash with water and neutralize with sodium chloride so that the pH of the 1% solution is 8.0, after which the product is dehydrated and crushed to obtain a comparative surfactant-6 as a yellow powder.
The properties of the coal-water slurry prepared with the addition of surfactants according to the invention and comparative surfactants as surfactants as dispersants are shown in Table. four.
Any surfactant according to the invention has a viscosity of less than 3000 cPa s
to
 20
thirty
Coziness and further, they modify by b, imetal-15 at a concentration of coal of 68% by weight of a platinum shock catalyst and show a better dispersing type for producing oils with a specific effect than comparative surfactants. with a weight of (15/4 ° С) 7883 g / cm3, interval - Example 2. Water-carbon suspensions 50–200 ° C, atomic ratio H / C of 1.48 and average mol.m. 100 3 then 1 ma.h. the starting material is placed in a glass autoclave in place with 2 m.ch. tetrachlorethylene, where (0.5 parts by weight of gasified anhydrous sulfuric acid is introduced at 15 ° C with stirring, with a frequency of 500 rpm {for sulphurization for 1 h. Then the temperature is raised to 50 ° C and oxidized by introducing 2 parts of gaseous nitrogen dioxide for 3 hours
Upon completion of this reaction, the content is cooled down to room temperature with unreacted oil-containing tetrachlorethylene1 and resinous. The reaction product is separated by a filter by separation and specific content is determined and the content of sulphonated ash is reduced to 2.1 wt.%
after which the water is evaporated by heating so that the non-solid substance is 80 wt.%. Water is then added to 100 g of the product and 0.5 g of the surfactant to obtain 71% by weight of the coal concentration. This mixture is treated in a disk mill for 5 minutes and the viscosity of the resulting suspension is measured with a 45 rotary viscometer. Comparative surfactant-6. 1 ma.ch. Comparative measurements are shown in the body-based surfactant-5, non-neutralized, high-concentration suspensions are prepared using the surfactants 1-30 according to the invention of Example 1, and comparative surfactants, after which their viscosity is measured.
about
Coal of the western CUA region with 25 humidity 3, -6 wt.%, Ash content 14.1 wt.%, Volatile substances 21.5 wt.% And carbon 58.1 wt.% Are ground in a finger mill and then ground in a disc mill. within 30 minutes in the form of a water-coal suspension with a concentration of 50% by weight to obtain a suspension with a particle size such that 78% of the particles pass through a 200 mesh screen.
Then, the suspension is desalt of methonyl groups and acid groups, which is equal to 0.5 mg eq / g and 7.3 mg.eq./g, respectively. The product is neutralized with caustic soda so that the pH of the aqueous solution of the product is 8.0 and after that the solution is adjusted to a 50% concentration, which served as a comparative surfactant-5 as a pale yellow liquid.
40
tab. five.
Alkali, placed in a glass autoclave and dispersed in 2 mash. purified water, to which is added 50 0.3 mas. 98% concentrated sulfuric acid and add 1 wt. H. 37% formaldehyde at 90 ° C and incubated for about 2 hours with stirring at a frequency of 500 rpm. After 5e, the mixture is kept at 100 + 2 ° C for 7 hours to carry out a condensation reaction. Upon completion of this reaction, the reaction product is filtered,
when the concentration of coal 68 wt.% and shows a better dispersing effect than the comparative surfactants. PRI mme R 2. Water-carbon sus-
the house of separation by specific gravity and ash content is reduced to 2.1 wt.%,
High concentrations of suspensions are prepared using surfactants 1-30 according to the invention of Example 1, and comparative surfactants, after which their viscosity is measured.
about
Coal of the western CUA region with a moisture content of 3, -6 wt.%, An ash content of 14.1 wt.%, Volatile substances of 21.5 wt.% And carbon of 58.1 wt.% Is ground in a finger mill and then triturated in a disk mill in for 30 minutes in the form of a water-coal slurry with a concentration of 50 wt.% to obtain a suspension with a particle size such that 78% of the particles pass through a 200 mesh screen.
Then, the suspension is de-ashed after which the water is evaporated by heating so that the solid substance is 80% by weight. Water is then added to 100 g of the product and 0.5 g of the surfactant to obtain 71% by weight of the coal concentration. This mixture is treated in a disk mill for 5 minutes and the viscosity of the resulting suspension is measured with a rotary viscometer. The measurement results are given in
tab. five.
Viscosity is measured at 20 ° C using a P 3 rotor at 12 rpm. Samples 2,4,4,8,9,11,13,16,19,20,21, 23,2,2,28 and 29 are placed in 1000 ml bottle and stored at room temperature for 6 months. When checking the glass rod in any of the bottles was not detected sediment.
At the same time, the surfactants according to the invention show good fluidity and viscosity less than 3500 cPa.s at 131338
coal concentration 71 wt.%, none of the comparative surfactants showed flowability of coal-water slurry.
Thus, the coal-water slurry prepared by the inventive method has a high coal concentration compared to slurries using conventional dispersants, while the coal-water slurry has good fluidity and stability at a concentration of 71 wt.% Coal.

权利要求:
Claims (3)
[1]
1. A method of producing a coal-water slurry by mixing fine coal, a dispersant and water, followed by homogenizing the mixture obtained, characterized in that, in order to reduce the viscosity of the suspension, the substance obtained by
BUT
A a a a
In In In With

Rootless
chamois
acid
60% oleum Bezvodna chamois
1 / 1.5
1 / 0.3 1 / 1.0
1 / 2.5 1 / 0.1
10X 1 / 4.0
61% 61%
61% 61%
1 / 6.0 1 / 3.5
1 / 4.0 1 / 5.0
14
Jq
five
0
by sulphurization of petroleum bitumen, or coal bitumen, or insoluble coal, or petroleum asphalt, or solvent deasphalting asphalt, or a mixture of petroleum and coal bitumen having a mol.m. 300-4250 and the ratio of H / C, 0.65-1.47, the subsequent oxidation of the resulting product and neutralization with alkali to obtain a neutralization product containing Ox5-7.9 mg Hectare / g of sulfonyl groups and 3.6 - 15 mg eq / g sour groups.
[2]
2. A method according to claim 1, characterized in that the sulfonation is carried out after the starting material is ground by anhydrous sulfuric acid in tetrachloroethane or tetrachloroethylene or perchlorethane.
[3]
3. A process according to claim 1, characterized in that the oxidation is carried out by nitrogen oxide.
Table I
5.1
10.3
7.4
1 / 6.0 1 / 3.5
1 / 4.0 1 / 5.0
Continuation of table 1
Table 3
Table 4
Not
yield 1350
980
1650
1540
1310
1150
970
860
720
650
740
1670
1850
940
1360
1020
1170
840
720
2010
1470
920
730
2640
1780
520
700
810
740
720
770
No fluidity
2420 No turnover
1140 No flow
980 No turnover
870 No turnover
920
No flow 1110
2120 1880
nineteen
1538901
g table
20

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引用文献:

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公开号 | 申请日 | 公开日 | 申请人 | 专利标题

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法律状态:

优先权:

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申请号 | 申请日 | 专利标题

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JP16323485|1985-07-23|

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