DE1646658B2 - Process for the production of carbon moldings of different, from the porous to the dense state reaching microstructure from modified pitch - Google Patents
Process for the production of carbon moldings of different, from the porous to the dense state reaching microstructure from modified pitchInfo
- Publication number
- DE1646658B2 DE1646658B2 DE1646658A DE1646658A DE1646658B2 DE 1646658 B2 DE1646658 B2 DE 1646658B2 DE 1646658 A DE1646658 A DE 1646658A DE 1646658 A DE1646658 A DE 1646658A DE 1646658 B2 DE1646658 B2 DE 1646658B2
- Authority
- DE
- Germany
- Prior art keywords
- modified pitch
- pitch
- microstructure
- porous
- achieve
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/515—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
- C04B35/52—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbon, e.g. graphite
- C04B35/528—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbon, e.g. graphite obtained from carbonaceous particles with or without other non-organic components
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
- C25B11/042—Electrodes formed of a single material
- C25B11/043—Carbon, e.g. diamond or graphene
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Electrochemistry (AREA)
- Inorganic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Structural Engineering (AREA)
- Ceramic Products (AREA)
- Carbon And Carbon Compounds (AREA)
- Working-Up Tar And Pitch (AREA)
Description
9 109 10
hatte leicht graphitierbare Eigenschaften, wie man der entsprechenden Gegenstände der vorangegangenerhad easily graphitizable properties, as one of the corresponding objects of the preceding
durch Röntgenstrahlen frttstellen konnte, und wies Beispiele ähnlich war und wies folgende Eigenschaf·by X-rays, and had examples similar and had the following properties
die folgenden Eigenschaften auf: ten auf:have the following properties:
Shore-Härte (Hs) 50 Shore-Härte (Hs) 115 bis 128Shore hardness (Hs) 50 Shore hardness (Hs) 115 to 128
Porosität 16% 5 Porosität 13%Porosity 16% 5 porosity 13%
Biegefestigkeit 290 kg/cm2 Schrumpfung 9 %Flexural strength 290 kg / cm 2 shrinkage 9%
Spezifischer Widerstand 6 · ΙΟ"4 Ohm · cm. Spezifisches Schüttgewicht... 1,50Specific resistance 6 · ΙΟ " 4 Ohm · cm. Specific bulk density ... 1.50
Carbonisationsausbeute 88 %Carbonization yield 88%
Beispiel 7 10 Biegefestigkeit 850kg/cir2.Example 7 10 Flexural strength 850kg / cir 2 .
Kohlenteerpech mit einem Erweichungspunkt von . .Coal tar pitch with a softening point of. .
850C wurde zu feinem Pulver gemahlen und in dieser Beispiel 985 0 C was ground to a fine powder and in this example 9
Form in einer Chlorgasatmosphäre auf 2500C erhitzt. 500 g Steinkohlenteerpech mit einem Erweichungs- Form heated to 250 0 C in a chlorine gas atmosphere. 500 g coal tar pitch with a softening
Das sich dabei ergebende Material hatte ein Wasser- punkt von 85°C wurden 90 min lang bei 400°CThe resulting material had a water point of 85 ° C and was kept at 400 ° C for 90 minutes
stoff/Kohlenstoff-Atomverhältnis von 0,38, und bis zu 15 trockendestilliert, wobei das Pech mit Luft abgeblasermaterial / carbon atomic ratio of 0.38, and up to 15 dry distilled, the pitch being blown off with air
einer Temperatur von 3600C war kein Erweichungs- wurde. Man erhielt ein modifiziertes Pech mit einema temperature of 360 ° C. was no softening. A modified pitch was obtained with a
punkt festzustellen. Erweichungspunkt von 23S bis 245°C und mit einempoint to be determined. Softening point from 23S to 245 ° C and with a
Dieses Material wurde anschließend in ein feines Wasserstoff/Kohlenstoff-Atomverhältnis von 0,46.This material was then converted into a fine hydrogen / carbon atomic ratio of 0.46.
Pulver gemahlen, das dann bei einem Druck von Dieses Pech wurde gemahlen und bei einem Druck vonPowder was ground, which was then ground at a pressure of This pitch was ground and at a pressure of
400 kg/cm2 zu dem gleichen Gegenstand gepreßt wurde 20 400 kg/cm2 zu einem Gegenstand geformt. Dei400 kg / cm 2 pressed into the same article, 20,400 kg / cm 2 was molded into an article. Dei
wie im Beispiel 4. Gegenstand wurde in Luft bei einem Temperatur-as in example 4. The object was in air at a temperature
Dieser Gegenstand wurde bei einem Temperatur- anstieg von 0,3°C/min auf 300"C erhitzt. DaraufThis object was heated to 300 ° C. with a temperature increase of 0.3 ° C./min
anstieg von 2 bis 3°C/min in Stickstoffgas auf 3000C folgte eine weitere Erhitzung auf 28OO°C mit einemincrease of 2 to 3 ° C / min in nitrogen gas to 300 0 C followed by a further heating to 28OO ° C with a
erhitzt und anschließend hitzebehandelt, indem er mit Temperaturanstieg von 5: C/min. Ein scheibenförmigeiheated and then heat-treated by using a temperature rise of 5 : C / min. A disc-shaped egg
einem Temperaturanstieg von 5°C/minauf eine höhere 25 Gegenstand mit einem Durchmesser von 40 mm unda temperature rise of 5 ° C / min to a higher object with a diameter of 40 mm and
Temperatur gebracht wurde. einer Dicke von 10 mm hatte eine Shore-Härte vorTemperature was brought. a thickness of 10 mm had a Shore hardness
Der sich ergebende Gegenstand hatte die gleiche 95, eine Porosität von 12% und eine BiegefestigkeitThe resulting article had the same 95%, a porosity of 12%, and a flexural strength
äußere Erscheinung wie die entsprechenden Gegen- von 600 kg/cm2.external appearance like the corresponding counterpart of 600 kg / cm 2 .
stände in den vorangegangenen Beispielen und wies Die Gitterabstände betrugen 3,39 A, zu deren Be-The lattice spacing was 3.39 A.
die folgenden Eigenschaften auf: 30 Stimmung die Rönteenstrahl-002-Beugungslinie be-the following properties: 30 moods the X-ray 002 diffraction line
Shore-Härte (Hs) 75 bis 85 Tf^u*' ^ ^?Ψ^α W t idersta?d 1^Shore hardness (Hs) 75 to 85 Tf ^ u * ' ^ ^? Ψ ^ α W t idersta ? d 1 ^
Porosität 20°/ 'cm' Endprodukt war ein Kohlen-Porosity 20 ° / ' cm ' End product was a carbon
Schrumpfung lgo/ Stoffmaterial mit schwieriger Graphitierbarkeit. Shrinkage lg o / material material with difficult graphitization.
Spezifisches Schüttgewicht... 1,35 Beispiel 10Specific bulk density ... 1.35 Example 10
Carbonisationsausbeute ....70% 35 . , , . .,„„„,-, A ..Carbonization yield .... 70% 35 . ,,. ., """, -, A ..
Bieeefestiekeit 400 ke/cm2 Petroleumasphalt wurde bei 390° C unter AnblasunjBieeefestiekeit 400 ke / cm 2 Petroleum asphalt was blown at 390 ° C
egeresugKeit U Kg/ m ' von Luft trockendestilliert. Das sich ergebende Mate-EgeresugKeit U Kg / m 'dry-distilled from air. The resulting material
. . rial wurde gemahlen und in einer Chlorgasatmosphärt. . rial was ground and left in a chlorine gas atmosphere
Beispiel 8 bei ejner Temperatur bis zu 25O0C hitzebehandelt For example 8 heat-treated at a temperature of up to 25O 0 C.
Der in Chloroform unlösliche Bestandteil eines 40 Das auf diese Weise gewonnene modifizierte PechThe chloroform-insoluble constituent of a 40 The modified pitch obtained in this way
Kohlenteerpechs wurde als Ausgangsmaterial benutzt. hatte ein Wasserstoff/Kohlenstoff-Atomverhältnis vorCoal tar pitch was used as the starting material. proposed a hydrogen / carbon atomic ratio
Dieses Material wurde in Pulverform gut ausgebrei- 0,42, und bis zu einer Temperatur von 36O0C war keirThis material was powdered well ausgebrei- 0.42, and up to a temperature of 36O 0 C was keir
tet, so daß es mit Luft in Berührung kam, und durch Erweichungspunkt festzustellen.tet so that it came into contact with air and determined by the softening point.
Erhitzen auf 2200C oxydiert. Hierbei erhielt man ein Dieses Pech wurde bei einem Druck von 300 kg/cnrHeat oxidized at 220 0 C. A This pitch was obtained at a pressure of 300 kg / cnr
Pech mit einem Wasserstoff/Kohlenstoff-Atomverhält- 45 in einen Gegenstand ausgeprägter Gestalt gepreßt, deiPitch with a hydrogen / carbon atomic ratio 45 pressed into an article of pronounced shape, the
nis von 0,50 und mit einem Erweichungspunkt von in Luft bei einem Temperaturanstieg von 1 °C/min aulnis of 0.50 and with a softening point of in air with a temperature rise of 1 ° C / min aul
245 bis 250°C. 300°C und anschließend in Stickstoff auf 2800°C245 to 250 ° C. 300 ° C and then in nitrogen to 2800 ° C
Dieses Pech wurde zu feinem Pulver zermahlen, das erhitzt wurde. Das auf diese Weise gewonnene Kohlen·This pitch was ground into a fine powder which was heated. The coal obtained in this way
bei einem Druck von 450 kg/cm2 zu einer Scheibe mit Stoffmaterial hatte eine Shore-Härte von 68, eine Poroat a pressure of 450 kg / cm 2 to a disk with fabric material had a Shore hardness of 68, a Poro
einem Durchmesser von 20 mm und einer Dicke von 50 sität von 48 %, eine Biegefestigkeit von 78 kg/cm2 unca diameter of 20 mm and a thickness of 50 sity of 48%, a flexural strength of 78 kg / cm 2 unc
7 mm gepreßt wurde. Die Scheibe wurde unter den einen spezifischen Widerstand von 13 · 10~3Ohm-cm7 mm was pressed. The disk was found to have a resistivity of 13 x 10 -3 ohm-cm
gleichen Bedingungen wärmebehandelt, wie es im Ferner wurde mit Röntgenstrahlen festgestellt, daß daiheat-treated under the same conditions as in the Further, it was found by X-rays that dai
Beispiel 5 angegeben ist. Der sich ergebende Gegen- Material schwierig zu graphitierende EigenschafterExample 5 is given. The resulting counter material has difficult to graphitize properties
stand hatte eine äußere Erscheinung, die derjenigen aufweist.stood had an outward appearance similar to that of one.
Claims (4)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP42006563A JPS5112474B1 (en) | 1967-02-03 | 1967-02-03 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| DE1646658A1 DE1646658A1 (en) | 1972-04-27 |
| DE1646658B2 true DE1646658B2 (en) | 1974-07-25 |
| DE1646658C3 DE1646658C3 (en) | 1975-03-13 |
Family
ID=11641783
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE1646658A Expired DE1646658C3 (en) | 1967-02-03 | 1968-02-03 | Process for the production of carbon molded bodies with different microstructure ranging from porous to dense state from modified pitch |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US3558276A (en) |
| JP (1) | JPS5112474B1 (en) |
| DE (1) | DE1646658C3 (en) |
| GB (1) | GB1220482A (en) |
Families Citing this family (35)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4016247A (en) * | 1969-03-31 | 1977-04-05 | Kureha Kagaku Kogyo Kabushiki Kaisha | Production of carbon shaped articles having high anisotropy |
| GB1260034A (en) * | 1969-08-12 | 1972-01-12 | Coal Industry Patents Ltd | Method of manufacturing unitary porous carbon bodies |
| US3888958A (en) * | 1970-03-21 | 1975-06-10 | Bergwerksverband Gmbh | Process for making shaped pieces from low temperature coke of low bulk weight |
| US3943213A (en) * | 1970-04-06 | 1976-03-09 | Great Lakes Carbon Corporation | Method for manufacturing high temperature graphite fiber-graphite composites |
| JPS55331B2 (en) * | 1972-09-14 | 1980-01-07 | ||
| US3917806A (en) * | 1973-09-27 | 1975-11-04 | Kureha Chemical Ind Co Ltd | Method for the preparation of carbon moldings and activated carbon molding therefrom |
| USRE29101E (en) * | 1972-09-30 | 1977-01-04 | Kureha Kagaku Kogyo Kabushiki Kaisha | Method for the preparation of carbon moldings and activated carbon moulding therefrom |
| US3919387A (en) * | 1972-12-26 | 1975-11-11 | Union Carbide Corp | Process for producing high mesophase content pitch fibers |
| US3919376A (en) * | 1972-12-26 | 1975-11-11 | Union Carbide Corp | Process for producing high mesophase content pitch fibers |
| US3995014A (en) * | 1973-12-11 | 1976-11-30 | Union Carbide Corporation | Process for producing carbon fibers from mesophase pitch |
| US4026788A (en) * | 1973-12-11 | 1977-05-31 | Union Carbide Corporation | Process for producing mesophase pitch |
| US4032430A (en) * | 1973-12-11 | 1977-06-28 | Union Carbide Corporation | Process for producing carbon fibers from mesophase pitch |
| JPS5331116B2 (en) * | 1974-01-31 | 1978-08-31 | ||
| US4032607A (en) * | 1974-09-27 | 1977-06-28 | Union Carbide Corporation | Process for producing self-bonded webs of non-woven carbon fibers |
| US4571317A (en) * | 1976-02-25 | 1986-02-18 | United Technologies Corporation | Process for producing binderless carbon or graphite articles |
| DE3125609A1 (en) * | 1981-06-30 | 1983-01-13 | Rütgerswerke AG, 6000 Frankfurt | METHOD FOR PRODUCING CARBON MOLDED BODIES |
| US4913889A (en) * | 1983-03-09 | 1990-04-03 | Kashima Oil Company | High strength high modulus carbon fibers |
| DE3464131D1 (en) * | 1984-03-23 | 1987-07-16 | Kawasaki Steel Co | Method for producing carbon powders |
| JPS60200816A (en) * | 1984-03-26 | 1985-10-11 | Kawasaki Steel Corp | Production of carbonaceous material |
| DE3563033D1 (en) * | 1985-01-18 | 1988-07-07 | Sigri Gmbh | Process for producing vitreous carton bodies |
| JPS6479073A (en) * | 1987-09-22 | 1989-03-24 | Petoca Ltd | Porous isotropic carbon-carbon composite material and its production |
| JPS6479079A (en) * | 1987-09-22 | 1989-03-24 | Petoca Ltd | Porous isotropic carbon-carbon composite material and its production |
| US6037032A (en) * | 1997-09-02 | 2000-03-14 | Lockheed Martin Energy Research Corp. | Pitch-based carbon foam heat sink with phase change material |
| US6780505B1 (en) * | 1997-09-02 | 2004-08-24 | Ut-Battelle, Llc | Pitch-based carbon foam heat sink with phase change material |
| US6033506A (en) * | 1997-09-02 | 2000-03-07 | Lockheed Martin Engery Research Corporation | Process for making carbon foam |
| US6673328B1 (en) | 2000-03-06 | 2004-01-06 | Ut-Battelle, Llc | Pitch-based carbon foam and composites and uses thereof |
| AU5034500A (en) * | 1999-05-20 | 2000-12-12 | Procter & Gamble Company, The | Method for removal of nano-sized pathogens from liquids |
| US7147214B2 (en) | 2000-01-24 | 2006-12-12 | Ut-Battelle, Llc | Humidifier for fuel cell using high conductivity carbon foam |
| KR100777951B1 (en) * | 2001-08-23 | 2007-11-28 | 더 프록터 앤드 갬블 캄파니 | Water filter material, corresponding water filter and method of use thereof |
| US7615152B2 (en) | 2001-08-23 | 2009-11-10 | Pur Water Purification Products, Inc. | Water filter device |
| US20050279696A1 (en) * | 2001-08-23 | 2005-12-22 | Bahm Jeannine R | Water filter materials and water filters containing a mixture of microporous and mesoporous carbon particles |
| US7614507B2 (en) * | 2001-08-23 | 2009-11-10 | Pur Water Purification Products Inc. | Water filter materials, water filters and kits containing particles coated with cationic polymer and processes for using the same |
| US7614508B2 (en) * | 2001-08-23 | 2009-11-10 | Pur Water Purification Products Inc. | Water filter materials, water filters and kits containing silver coated particles and processes for using the same |
| RU2734685C1 (en) * | 2019-09-17 | 2020-10-22 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Казанский национальный исследовательский технический университет им. А.Н. Туполева-КАИ" (КНИТУ-КАИ) | Method of making articles from carbon-carbon composite material |
| CN112458490B (en) * | 2020-11-24 | 2024-07-16 | 吉林科工碳业有限公司 | Fluorine-producing anode and preparation method thereof |
-
1967
- 1967-02-03 JP JP42006563A patent/JPS5112474B1/ja active Pending
-
1968
- 1968-01-31 US US701827*A patent/US3558276A/en not_active Expired - Lifetime
- 1968-02-02 GB GB5348/68A patent/GB1220482A/en not_active Expired
- 1968-02-03 DE DE1646658A patent/DE1646658C3/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| GB1220482A (en) | 1971-01-27 |
| DE1646658A1 (en) | 1972-04-27 |
| DE1646658C3 (en) | 1975-03-13 |
| JPS5112474B1 (en) | 1976-04-20 |
| US3558276A (en) | 1971-01-26 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C3 | Grant after two publication steps (3rd publication) | ||
| E77 | Valid patent as to the heymanns-index 1977 |