• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Carbon blacks having a carbon content greater than 99%, a mean particle diameter of 250 to 300 A, an electrical resistivity, measured under a pressure of 6.3 bars, of 0.270 to 0.350 ohm.cm and a DBP index of 400 to 500 ml per 100 g of black are disclosed together with a process for their preparation by incomplete combustion of acetylene in air. These blacks may be used especially for the manufacture of electric cells.
    公开号:SU791255A3
    申请号:SU782588152
    申请日:1978-03-07
    公开日:1980-12-23
    发明作者:Жие Клод
    申请人:Продюи Шимик Южин Кюльман (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to the production of acetylene black, used mainly in the manufacture of galvanic cells. A method of producing acetylene black is known, which involves burning acetylene with air at a molar ratio of oxygen to acetylene of 0.250, 9 at a pressure above atmospheric. However, this method cannot produce carbon black with a high electrical conductivity and structure. The closest to the present invention is a method for producing acetylene black, including preheating the oxygen stream to 320 ° C and hydrocarbon gas (, CH (,) to a temperature close to the temperature of their thermal decomposition, and the subsequent incomplete combustion of the hydrocarbon in the furnace A good ratio of oxygen to hydrocarbon is less than 1 (0.4-0.5) at a pressure below atmospheric pressure. The disadvantage of this method is to obtain carbon black only with a specific electrical resistance not lower than 0.4 ΩSM and structural (coefficient of DBP) not more than 320 mland 100 g of carbon black. The purpose of the invention is to improve the structure and electrical conductivity of carbon black. This goal is achieved by the fact that the proposed method, including preheating carbon and oxygen-containing gas streams and the subsequent incomplete combustion of hydrocarbon in a furnace at a pressure below atmospheric and the release of soot, acetylene is used, air preheated to 600-850 ° C is used as oxygen-containing gas, and combustion is carried out at a molar ratio of oxygen to acetylene of 0.08-0.20, acetylene It is heated to a temperature of not more than 100 ° C and the walls of the furnace are heated to 1500 ° C. The proposed method produces acetylene black with higher characteristics, that is, with a specific electrical resistance, measured at a pressure of 6.3 bar, less than 0.3 ohm-cm and with a DVR coefficient greater than 320 ml per 100 g of carbon black. Incomplete combustion occurs. as follows: the acetylene is preheated in the furnace (the walls of which are heated externally or not) is brought into contact with the air preheated to a temperature higher than or equal to 600 ° C, and the molar ratio of the introduced acetylene and air is 0.08-0.20.
    The preheat temperature of acetylene does not exceed, and the air -.
    The walls of the furnace is usually not heated outside. Preferably, the furnace walls are maintained in the zone where acetylene black is formed at a temperature higher than or equal to 1500 ° C by supplying heat from the outside. The temperature at which the furnace walls are maintained does not exceed 20000 s (out 2300 ° C).
    The air flow is introduced into the furnace in the zone immediately adjacent to the zone of introduction of acetylene flow, to the periphery and tangentially to it.
    Incomplete combustion of acetylene occurs in the upper part of a vertical furnace, the walls of which are heated or not electrically. The aerosol formed by the soot particles and the residual reaction gases is directed along the line in which the aerosol is cooled by natural convection, and through the fan into the cyclones - separators, and the soot is collected in the bunker.
    During the continuous flow of the process, the acetylene current is interrupted from time to time for a very short time (from several seconds to a minute) and during this interruption a stream of compressed air is introduced into the furnace to separate the gas soot that is fixed to the walls of the furnace.
    The soot temperature is 2000 ° C. Acetylene black, obtained by the proposed method, has a high crystalline ordering and a highly developed structure. Roy.
    The properties of acetylene blacks {the average particle diameter and specific surface area (or surface determined by the BET method) are determined respectively by examination under an electron microscope and by nitrogen adsorption.
    Electrical resistivity is defined as
    Soot is placed in. a cylindrical, non-transmitting tube containing in its lower part a metal cap forming the electrode. A metal piston is placed above the soot, the end of which forms another electrode. This piston is affected by a pressure of 6.3 bar. The amount of soot introduced into the cylinder takes a height of 1.5 cm under pressure. Two electrodes are connected to the Wheatstone bridge and the electrical resistance is measured: a soot column. The resistivity of soot is determined by the formula
    (S / J), where R is expressed in ohms;
    S - is the cross-section of a column (column), expressed in cm, g
    3 .- means the height of the pillar (column), expressed in cm.
    The absorption capacity with respect to liquids, which is to some extent a measure of the structure of soot, is characterized by data of various indicators (coefficients), in particular the filtration index and the DBP index.
    The filtration rate is determined as follows.
    The carbon black is preliminarily passed through a sieve, the holes in the cells of which are 0.074 mm, 5 g of the screened carbon black are moistened with a water-acetone mixture containing 3 wt.% Acetone to obtain a slurry. The slurry is filtered on a Buchner funnel under a vacuum of 200 mm water column. A layer of soot formed at the bottom of the Buchner funnel, after removing most of the water, is wrung out, leaving it for 20 minutes on the Buchner funnel, maintaining the vacuum of 200 mm of water all the time. Art. The weight of the water-acetone mixture absorbed by 5 g of carbon black is then determined by weighing. This weight is called the filtration rate.
    The DBPD value is determined according to the French Standard NF T 45-122 method, modified as follows;
    For each sample of acetylene soot, 7 measurements of the DBP indicator are made, respectively, taken to test 1,2,3,4,5,6 and 7 g of carbon black, and a curve of the DBP indicator (expressed in ml per 100 g of carbon black) f ( weight taken); this curve has an inflection point; The preferred value for DBP is the value corresponding to the inflection point.
    In tab. 1 presents the comparative characteristics of the known and proposed acetylene black.
    Properties Carbon content,% Average particle diameter, A 250-300 Specific surface area, Specific resistance. Ohm-cm Indicator of fnltratsii Indicator DVR {ml. per 100 g of carbon black) Example 1. 40 standards were introduced into a vertical furnace through a nozzle. acetylene, preheater but not preheated, and 40 nfrm. air preheated to 800 ° C (with respect to O tCjHj 0,2). The walls of the upper part of the furnace are not electrically heated. Every 30 minutes, the flow of acetylene is interrupted for 1 minute and air is directed into the oven at room temperature, compressed under a pressure of 2 bar. Then again let the current acetylene. The reaction starts again during this recovery process. The pressure in the furnace is 200 mm of water. Art. In this way, 34 kg / h of acetylene black, having an electrical resistivity of 0.295 ohm-cm and a DBF of 460 ml per 100 g of carbon black, is obtained. The crystal lattice parameters (the average height L of the crystal layers, the average diameter of the L layers, the C / 2 distance between the two planes of the resulting acetylene black soot are determined by X-ray diffraction (X-rays). Table 2 shows the lattice parameters. Table of Table Parameters Offered soot The crystal structure of the proposed soot approaches that of graphite (for C / 2 graphite 3.41 S)., Example 2. The analogs of example 1 are carried out, except for that.
    Table 1
    Offered soot Known
    权利要求:
    Claims (2)
    [1]
    carbon black 100-120 0.270-0, 100-120 400-500 99 50-200 85-115, 400-0,700 80-85 that 50 norms were introduced into the furnace through the nozzle. acetylene, preheated before and 20 standards. air, preheated to (with respect Op: SpNp 0.08). 49 kg / h of acetylene black are obtained, having a DBP of 400 ml per 100 g of carbon black and an electrical resistivity of 0.250 Ohm.cm. Example 3. 50 n.m./h of acetylene, not preheated, and 20 n.m./h of air, preheated to 700 ° C (at a C2H ratio, j, 0.08), are introduced through a nozzle into a vertical furnace. The walls of the upper part of the furnace are maintained by electrical heating at a temperature close to. Every 30 min the current of acetylene is interrupted for 10 seconds and compressed under a pressure of 2 bar is introduced into the oven and at room air temperature. Then again let the current acetylene. 49 kg / h of acetylene black are obtained, having a DBP of 500 ml per 100 g of carbon black and an electrical resistivity of 0.270 ohm-cm. Claim 1. Method for producing acetylene black, including preheating hydrocarbon and oxygen-containing gas streams and subsequent incomplete combustion of hydrocarbon in a furnace at a pressure below atmospheric and soot evolution, characterized in that acetylene is used as a hydrocarbon gas to improve structural and electrical conductivity. , as an oxygen-containing gas — air preheated to 600–850 ° C, and 7,791 combustion is carried out at a molar ratio of oxygen to acetylene 0.08–0.20. 2. The method according to claim 1, distinguishes with the fact that acetylene is preheated to a temperature of no more. 3. Method according to paragraphs. 1 and 2, which is based on the fact that the walls of the furnace are heated to 1500 s. 2558 Sources of information taken into account in the examination 1. UK patent 1149908, cl. C 09 S 1/48 (CED), published. 04/23/69.
    [2]
    2. For France of France No. 2229744, cl. C 09 C 1/54, published. 12.13.74 (prototype).
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    同族专利:
    公开号 | 公开日
    BR7801430A|1978-10-10|
    IN149003B|1981-08-15|
    IT7867500D0|1978-03-09|
    DE2809280A1|1978-09-14|
    AU518710B2|1981-10-15|
    RO75063A|1980-10-30|
    DE2809280C2|1990-10-04|
    CA1113691A|1981-12-08|
    JPS53110992A|1978-09-28|
    DD135394A5|1979-05-02|
    ES467723A1|1978-10-16|
    NO780797L|1978-09-12|
    PL110648B1|1980-07-31|
    FR2383215A1|1978-10-06|
    NL185940C|1990-08-16|
    NL7802461A|1978-09-12|
    PL205117A1|1979-03-26|
    IT1109126B|1985-12-16|
    GB1597857A|1981-09-16|
    NL185940B|1990-03-16|
    NO144889C|1981-12-02|
    NO144889B|1981-08-24|
    FR2383215B1|1980-01-04|
    BE864472A|1978-09-04|
    US4279880A|1981-07-21|
    PH15770A|1983-03-24|
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    BE465176A|
    AT149666B|1935-05-17|1937-05-25|Ig Farbenindustrie Ag|Process and apparatus for the production of carbon black.|
    GB493929A|1936-01-09|1938-10-17|Bayerische Stickstoffwerke Ag|An improved process for making carbon black, which is poor in impurities, and hydrogen or hydrogen-containing gases|
    US2453440A|1943-05-11|1948-11-09|Shawinigan Chem Ltd|Carbon black|
    FR1021995A|1950-07-12|1953-02-26|Soc Produits Azotes Sa|Carbon black with high thermal conductivity and its manufacturing process|
    US2690960A|1951-05-09|1954-10-05|Cabot Godfrey L Inc|Detonation process of making carbon black|
    US3124529A|1959-03-17|1964-03-10|Process for the treatment of fluids |
    FR1462071A|1964-12-30|1966-02-25|Cabot Corp|Conductive carbon blacks and process for making them|
    DE1592864C3|1967-08-11|1975-05-22|Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler, 6000 Frankfurt|Method of making FurnaceruB|
    FR2229744B1|1973-05-15|1976-11-12|Ugine Kuhlmann|US4351815A|1979-06-11|1982-09-28|Columbian Chemicals Company|Battery carbon black|
    JPS5938993B2|1980-03-11|1984-09-20|Denki Kagaku Kogyo Kk|
    JPS5839458B2|1980-10-28|1983-08-30|Denki Kagaku Kogyo Kk|
    EP0069004B1|1981-06-26|1986-10-15|Societe Les Piles Wonder|Cathodic mixtures for dry manganese dioxide-zinc batteries with a salty electrolyte|
    FR2508710B1|1981-06-26|1985-12-27|Wonder|IMPROVEMENT IN CATHODE MIXTURES OF DRY CELLS WITH MANGANESE-ZINC BIOXIDE WITH SALINE ELECTROLYTE|
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    JPH0427673B2|1983-11-22|1992-05-12|Denki Kagaku Kogyo Kk|
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    JPH0158227B2|1984-04-05|1989-12-11|Denki Kagaku Kogyo Kk|
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    JPH0411519B2|1984-11-21|1992-02-28|
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    CN1052579C|1996-06-04|2000-05-17|彭崇恩|Mfg. of rechargeable corpuscular accumulator|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7706894A|FR2383215B1|1977-03-09|1977-03-09|
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