[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

GB2188311A - Process for modifying the surface characteristics of carbon black - Google Patents

Process for modifying the surface characteristics of carbon black Download PDF

Info

Publication number
GB2188311A
GB2188311A GB08705181A GB8705181A GB2188311A GB 2188311 A GB2188311 A GB 2188311A GB 08705181 A GB08705181 A GB 08705181A GB 8705181 A GB8705181 A GB 8705181A GB 2188311 A GB2188311 A GB 2188311A
Authority
GB
United Kingdom
Prior art keywords
carbon black
alkane
adsorbate
surface area
black
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
Application number
GB08705181A
Other versions
GB8705181D0 (en
GB2188311B (en
Inventor
Jaspard Harvey Atkins
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Cabot Corp
Original Assignee
Cabot Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Cabot Corp filed Critical Cabot Corp
Publication of GB8705181D0 publication Critical patent/GB8705181D0/en
Publication of GB2188311A publication Critical patent/GB2188311A/en
Application granted granted Critical
Publication of GB2188311B publication Critical patent/GB2188311B/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C1/00Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
    • C09C1/44Carbon
    • C09C1/48Carbon black
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • C08K9/04Ingredients treated with organic substances
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C1/00Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
    • C09C1/44Carbon
    • C09C1/48Carbon black
    • C09C1/56Treatment of carbon black ; Purification
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/12Surface area

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Pigments, Carbon Blacks, Or Wood Stains (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The surface characteristics of a furnace carbon black having a nitrogen surface area greater than 140 m2/g, are modified by treating the black with an organic adsorbate (eg. an n-alkane, n-alkane amine, n-alkane halide or n-alkane alcohol) having a molecular structure including a linear chain having at least four carbon atoms at a loading ranging from 1 to 2 percent by weight, whereby carbon black pores can be filled to effectively block adverse moisture absorption.

Description

SPECIFICATION Process for modifying the surface characteristics of carbon black and carbon black produced thereby Carbon black is produced by the thermal decomposition of hydrocarbons at very high temperatures. The blacks so formed are composed of essentially elemental carbon in the form ofaggregated particles of colloidal dimensions and high surface area. All carbon blacks, regardless of the method of manufacture or raw materials used in their production, possess many similar properties. The distinction between the various types or grades of carbon blacks is one of degree rather than kind, and is based on such characteristics as particle size, surface area, chemical composition ofthe particle surface, and extent of particle to particle association.
The carbon black particles generally are porous and feature both external and internal surface areas.
Specific surface areas, typically evaluated by adsorption techniques, commonly are used to identify and classify the blacks. Various product performance characteristics have been attributed to the internal and/or external surface areas of the carbon blacks incorporated therein.
Carbon black is a widely used ingredient for imparting conductivity to polymer systems. One such application is in anti-static compounds, such as for sheeting, belting, hoses, and molded goods, in order to minimize static build-up and explosion hazards in environments such as mines, hospitals, and other areas where solvent vapors or oxidants may collect. In the wire and cable industry, conductive carbon black compounds are utilized as metal conductor strand shielding in high voltage cables.
When carbon black is incorporated into polymer systems, however, the compound moisture absorption (CMA),the amount of moisture absorbed by the compound, may increase. The increase in CMA in conductive polymers can contribute to at least two significant problems. Firstly, the moisture absorbed in the compound can be vaporized during the extruding operations where temperatures can exceed 100 C (373"K). This vaporization results in "blow-holes" on the surface of the extrudate, which are a potential source of dielectric weakness.Secondly, the moisture absorbed in the compound can itself initiate dielectric breakdown by a process referred to in the art as "treeing". (The descriptive term "treeing" is derived from the shape of dielectric breakdown pathways as observed by rnicroscopic examination.) In particular, when certain conductive blacks are compounded into polymeric materials, the increase in CMA has been found to be primarily attributableto the microporosity of the carbon black. Now, according to the present invention, a process has been discovered whereby the microporosity of a carbon black can be selectively modified. The carbon black is treated with an organic adsorbate which is adsorbed by the black and effectively blocks micropores in a specific size range, while not adversely affecting other compound properties.
Applicant has determined that by treating a carbon black with an adsorbate, featuring select molecular dimensions, pores of a select diameter range can be filled and thereby effectively block adverse moisture absorption. It was found that the molecules of select adsorbate become firmly bound to the carbon black and do not become liberated under normal handling, storage, or use conditions. Theory suggests that the over lapping potential fields present in such small pores bind the adsorbate molecules with relatively high en- ergies making it difficult to displace the molecule from the micropore.
The treatment according to the present invention may be effectively applied to any grade of carbon black having a surface micro-structure featuring a significant portion of micropores in the size range penetrable by molecules of water. The black may be in pelleted orfluffyform. Accordingly, the treatment has been found to produce favorable results in modifying high surface area furnace blacks (having a nitrogen surface area [N2SA] greater than about 140 m2/g), since these blacks appear to feature a surface micro-structure with a significant portion of micropores in the specified size range. Effective results have been accomplished in treating preferred furnace blacks having a N2SA ranging from about 200 m2/g to about 260 m2/g.
The adsorbate of the present invention may be any organic molecule including a linear chain having at leastfourcarbon atoms, such as alkanes and substituted alkanes (amines, halides, alcohols, and the like) and mixtures thereof. Typical materials include n-octane, n-amino octane, n-hexanol, n-bromo octane, n-chloro octane, 4 methyl heptane, 2-5 dimethyl heptane, 2-3-4trimethyl pentane, 2-2-4trimethyl pentane, hexamethyl ethane, n-nonane, n-decane, n-dodecane, n-hexadecane, 1-3 dichloro propane, and the like. For reasons of efficiency and permanance of treatment during heat processing, adsorbatesfeaturing a linear chain of at least ten carbon atoms are preferred.Particularly preferred are n-alkanes, C10-C15, which feature thermal stability to above about 2500C (523"K).
The manner in which the adsorbate is applied to the carbon black is not critical. Typically, the treatment simply consists of mixing the chosen amount of adsorbate with the black in a suitable vessel and then agitating the black to ensure adsorbate impregnation of the blacksurface. Excess or unadsorbed adsorbate can be removed by drying the treated black at moderate temperatures, typically ranging from about 100to 200"C (373 to 473on). Treatment of the black also may conveniently be incorporated into various process steps during manufacture or utility of the carbon black.For example, a suitable adsorbate may be injected into the process stream of a carbon black reactor prior to collection of the black, or, the adsorbate may be introduced during a compounding operation as a black is beirig blended with a polymer.
The optimum amount of adsorbate to be used depends on the darbon blackto be treated, its surface area, and the percentage ofthat surface area consisting of micropores in the size range effectively blocked bythe adsorbates of the present invention. When treating conductive carbon black, effective results have been accomplished using about 0.5 to about 5 percent by weight adsorbate; about 1.0 to about 2.0 percent adsorbate is particularly preferred.
The following examples are provided to further illustrate the invention. The examples are intended to be illustrative in nature and are not to be construed as limiting the scope of the invention.
Test pro cedures An amount of carbon black was weighed into a glass jar and a measured percent by weightofadsorbate then was added to the black. The jar was sealed with a lid and the contents were thoroughly mixed by rolling the jar for about one to five minutes (60to 300 seconds). After loosening the lid, the jar and its contents were then placed in an overto dry.
In orderto evaluate the performance characteristics of the blacks in imparting compound moisture adsorp- tion and volume resistivity properties, the blacks were compounded with a suitable resin. For purposes of illustration, an ethylene/ethyl acrylate (EEA) was used as the resin in the following examples. The compound to be tested was prepared by incorporating the desired amount of black into the resin, on a weight percent basis. The blacks were compounded, at specified loadings, into the EEA using a Brabender mixer running at 60 RPM with circulating oil at 11 0 C (383"K) for nine minutes (540 seconds). The resulting compound was sheeted on a cold two-roll mill and formed into sheets forthe subsequenttesting.
In orderto determine CMA, sheets of the various ethylene/ethyl acrylate (EEA) compounds were diced or cut into pellets two yield suitable granulated test samples. Athree gram sample ofthe granulated compound was weighed into a glass crucible of known weight and dried at 600C t 3" (333"K) and 1/3 atomsphere (3.4 x 1 04 Pa) for two hours (7200 seconds) to remove moisture from the compound. After cooling in a desiccator, the weight was obtained to the nearesttenth of a milligram.The compound then was placed into a desiccator maintained at conditions of room temperature (70 + 2"F [294 K]) and 79 percent relative humidity (R.H.)for48 hours (1.728 x 1 seconds). The compound then was weighed after 30 minutes (1800 seconds) and periodically at 24 hour (8.64 x 1 seconds) intervals until constant weight (0.03 percent increase in CMA) was achieved.The equilibrium moisture absorptoin was calculated as a weight percentage of the compound using the following formula: CMA(wt%)=(C+S)-(C+DS)-B x 100 (C + DS) - (TC) wherein C+S = final weight container + sample C + DS = weightcontainer + drysample TC = tare weight glass crucible B = change in weight blankcontainer Volume resistivity of a material is the ratio of the potential gradient parallel to the current in the material to the current density. Volume resistivity is measured in ohms centimeter; it is the reciprocal ofvolume conductivity.In order to determine the volume resistivity of plastic compounds containing carbon black, sam- pleswere prepared by molding standard 80 mil tensile plaques from the millsheets and 2" x 6"(5.1 x 15.2cm) .electrical test specimens were cut out of the tensile plaques. Each specimen was coated with a silver paint (silver conductive coating in ethyl alcohol) to produce a one-half inch (1.27 cm)wide silver electrode at each end.The specimens were placed in a sample holder (between 8 x 6 [20.3 x 15.2 cm] glass plates arranged crosswiseto each othersuch that the edge ofthetop plate is evenly lined with the edge of the specimen) and the electrodes attached to a Leeds and Northrup test set (#5035) consisting of a Wheatstone Bridge and Galvanometer. The voltage impressed on the test specimens was approximately 4.5 volts. The DC resistances across the length of the sample were measured and converted to Volume Resistivity in ohm-cm using thefollowing formula: Volume Resist (ohm-cm) = 2 x T x (2.54) x R 5x(2.54) wherein T = thickness of sample (inches) R = resistance (ohms) 2.54 = conversion constant (in. cm) 5 = distance constant (inches) - measure of the distance between the two one-half inch silver electrodes painted on each end of the test specimen The resistance of the specimen was measured in an oven maintained at 900C (363"K). In doing so,the resistance initially was measured after three minutes (180 seconds) at 90"C (3630K) with subsequent readings being taken at two minute (120 second) intervals for the next 30 minutes (1800 seconds).After 30 minutes (1800 seconds) readings were taken every five minutes (300 seconds) until the specimen had been in the 90 C (363 K) oven for a total of 60 minutes (3600 seconds). The value forthe resistance of the specimen at90 C (363"K) was fixed on a plot as the point at which the readings became constant.
Nitrogen surface area (N2SA) of the carbon black samples was determined in accordance with ASTM Test Method D3037-76, Method C, and is expressed in terms of square meters per gram (m2/g).
The table below iist representative results obtained using a selection of blacks and absorbates.
Tables land II list results with two different carbon black samples and using varying amounts oftwo adsorbates.
The data shown in Table Ill indicates that treatment with homologs of n-alkanes demonstrate comparable beneficial results. Increasing the chain length of the adsorbate has the benefit of offering higher atmospheric boiling points and highertemperature stability against desorption.
Table IV reports the effects of treatment using various isomers of octane. The adsorbate molecules all feature the same molecular formula but exhibit increasing degrees of branching moving from the top to the bottom of the table. While treatmentwith all of the adsorbates demonstrated beneficial results, linear molec- ules were most effective.
Table V lists treatment results from using various adsorbates, including both substituted and unsubstituted alkanes. The amines and alcohols appear two have a slight affinityforwaterwhich is not presentforthe halogenated and unsubstituted alkanes.
Table VI reports the results wherein carbon blacks of varying surface areas were treated. The example employing a low surface area black (about 50 m2/gm) evidenced no effect when treated pursuantto the present invention.
Table Vll reports results wherein carbon blacks of varying surface areas were treated with varying amounts of n-decane adsorbate.
Tablet Compound: Carbon Black* (36% Loading) in EEA Volume Adsorbate Treatment CMA Resistivity (wt%) Conditions (wt%) 25"C 90"C CONTROL 0.66 3.12 13.5 3% n-octane 150 C/60min 0.29 2.76 10.8 CONTROL 0.63 2.75 11.5 1.5% n-octane 150 C/60min 0.29 2.59 10.3 *The carbon black was VULCAN XC-72 (ASTM-N-472), a conductive carbon black available from Cabot Corporation, having a nitrogen surface area of about 215-260 m2/g.
Table COMPOUND: Carbon Black* (36% Loading) in EEA Volume Adsorbate Treatment CMA Resistivity (wt%) Conditions (wt%) 25"C 90"C CONTROL 150"C/60 min 2.45 1.9 5.1 3% n-octane " 0.92 2.2 5.1 4.5% n-octane " 0.43 2.1 6.0 CONTROL 2.49 1.9 5.6 3% n-octane " 1.08 1.6 3.9 4.5% n-octane " 0.55 2.1 6.0 *The carbon black used had a nitrogen surface area of about 610 m2/g.
Table 111 COMPOUND: Carbon Black* (36% Loading) in EEA Volume Adsorbate Treatment CMA Resistivity (wt%) Conditions (wt%) 25 C 90 C CONTROL 0.56 3.3 10.4 1 n-octane 200 C/12hrs 0.22 2.8 9.1 1 1/2%n-decane " 0.23 2.9 8.7 1 1/2%n-dodecane " 0.24 3.2 10.1 1 1/2%n-hexadecane " 0.24 3.2 10.3 Table IV COMPOUND:Carbon Black* (36% Loading) in EEA Volume Adsorbate Treatment CMA Resistivity (wt%) Conditions (wt%) 25 C 90 C CONTROL 200 C/12hrs 0.66 2.9 9.6 1.5% n-octane " 0.20 2.8 9.1 1.5% 4 methyl heptane " 0.28 3.1 11.5 1.5%2-5dimethyl heptane , 0.28 3.3 10.1 1.5% 2-3-4trimethyl pentane " 0.35 3.2 10.5 1.5% 2-2-4trimethyl pentane D 0.38 2.7 8.5 1.5% hexamethyl ethane " 0.44 5.4 25.5 *The carbon black used was VULCAN XC-72 (ASTM-N-472), a conductive carbon black available from Cabot Corporation, having a nitrogen surface area of about 215-260 m2/g.
Table V COMPOUND: Carbon Black* (36% Loading) in EEA Volume Adsorbate Treatment CMA Resistivity (wt%) Conditions (wt%) 25 C 90"C CONTROL 0.65 2.8 12.2 1% n-octane 150 C/50min 0.29 2.6 10.3 3% n-amino octane " 0.34 3.6 17.4 2%n-hexanol 150 C/12hrs 0.44 3.0 14.0 CONTROL 0.77 4.5 31.9 2% n-octane 110 C/60min 0.36 3.7 17.1 2%n-decane " 0.32 3.7 18.1 2% n-bromo octane " 0.38 3.9 19.5 2% n-chloro octane " 0.33 3.3 14.6 1.5%1-3dichloropropane " 0.30 2.8 9.3 *The carbon black used was VULCAN XC-72 (ASTM-N-472), a conductive carbon black available from Cabot Corporation, having a nitrogen surface area ofabout 215-260 m2/g.
Table VI COMPOUND: Carbon Black (36% Loading) in EEA Volume Adsorbate N2SA Loading Treatment CMA Resistivity (wt%) (m2/gm) (wt%) Conditions (wt%) 25"C 90"C CONTROLA 50 36 150"C/60min 0.38 4.1 74 1.5% Norpar 121 36 " 0.38 4.2 76 CONTROL 8 138 36 8 0.44 3.5 21 1.5% Norpar 12 36 " 0.27 3.9 21 CONTROL C 224 36 " 0.78 2.6 11 1.5% Norpar 12 36 " 0.46 2.6 9 1.5% Norpar 122 36 N/A 0.52 2.2 8 CONTROLD 635 14 150 C/60min 1.03 45 146 4.5% n-nonane 14 " 0.22 56 192 CONTROLS 810 14 " 0.45 9 26 3%n-decane 14 " 0.26 11 27 CONTROL 1727 12 " 0.33 16 19 3%Norpar12 12 " 0.11 15 18 (1) Norpar 12 is a mixture of n-alkanes having an average of 12 carbons (commercially availablefrom Exxon Company USA).
(2) In this example, the adsorbate was introduced during the carbon black/EEA compounding operation.
Table VII COMPOUND: Carbon Black (36% Loading) in EEA Volume Adsorbate N2SA Loading Treatment CMA Resistivity (wt%) (m2/gm) (wt%) Conditions (wt%) 90"C CONTROL1 142 36 150"C/60min 0.49 34.2 .75% n-decane 36 " 0.37 34.7 CONTROL2 235 36 " 0.78 16.7 1.5%n-decane 36 " 0.39 13.0 CONTROL3 1052 14 " 0.45 26.0 3%n-decane 14 " 0.26 26.5 CONTROL4 1322 14 " 0.63 19.2 3% n-decane 14 " 0.38 20.6

Claims (11)

1. A method for modifying the surface characteristics of a furnace carbon black having a nitrogen surface area greaterthan 140m2/g comprising treating the surface of said carbon black with an organic adsorbate having a molecular structure including a linear chain having at least four carbon atoms.
2. The method of claim 1 wherein said carbon black has a nitrogen surface area ranging from 200 to 260 m2/g.
3. The method of claim 1 wherein said carbon black is treated with an organic adsorbate comprising an n-alkane, n-alkane amine, n-alkane halide or n-alkane alcohol.
4. The method of claim 3 wherein the organic adsorbate is an n-alkane having 10 to 16 carbon atoms, or mixture thereof.
5. The method of claim 4wherein said carbon black having nitrogen surface area ranging from 200 to 260 m2/g is treated with adsorbate at a loading ranging from 1 to 2 percent byweight.
6. A modified carbon black obtained by treating a furnace carbon black having a nitrogen surface area greater than 140 m2/g with an organic adsorbate including a linearchain having at least four carbon atoms.
7. The carbon black of claim 6 wherein the organic adsorbate is an n-alkane amine, n-alkane, n-alkane halide or n-alkane alcohol.
8. The carbon black of claim 6wherein the organic adsorbate is an n-alkane having lotto 16 carbon atoms or mixtures thereof.
9. The carbon black of claim 6 obtained by treating a carbon black having a nitrogen surface area ranging from 200 to 260 m2/g.
10. The carbon black of claim 8 obtained by treating a furnace carbon black having a nitrogen surface area ranging from 200 to 260 m2/g with adsorbate at a loading ranging from 1 to 2 percent byweight.
11. A method for modifying the surface characteristics of a furnace carbon black as claimed in claim 1 and substantially as herein described with reference to the Examples.
GB8705181A 1986-03-24 1987-03-05 Process for modifying the surface characteristics of carbon black and carbon black produced thereby Expired - Fee Related GB2188311B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US84344586A 1986-03-24 1986-03-24

Publications (3)

Publication Number Publication Date
GB8705181D0 GB8705181D0 (en) 1987-04-08
GB2188311A true GB2188311A (en) 1987-09-30
GB2188311B GB2188311B (en) 1990-10-24

Family

ID=25289998

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8705181A Expired - Fee Related GB2188311B (en) 1986-03-24 1987-03-05 Process for modifying the surface characteristics of carbon black and carbon black produced thereby

Country Status (27)

Country Link
JP (1) JPS62275164A (en)
KR (1) KR950006688B1 (en)
CN (1) CN1025863C (en)
AR (1) AR245760A1 (en)
AU (1) AU599087B2 (en)
BE (1) BE906089A (en)
BR (1) BR8701003A (en)
CZ (1) CZ281256B6 (en)
DD (1) DD258996A5 (en)
DE (1) DE3703077A1 (en)
DK (1) DK147287A (en)
ES (1) ES2004891A6 (en)
FR (1) FR2596055B1 (en)
GB (1) GB2188311B (en)
HU (1) HU200613B (en)
IL (1) IL81236A (en)
IN (1) IN168779B (en)
IT (1) IT1203367B (en)
LU (1) LU86811A1 (en)
MX (1) MX168266B (en)
NL (1) NL8700664A (en)
NZ (1) NZ219110A (en)
PL (1) PL152526B1 (en)
PT (1) PT84488B (en)
SE (1) SE465464B (en)
YU (1) YU44613B (en)
ZA (1) ZA87118B (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996018456A2 (en) * 1994-12-15 1996-06-20 Cabot Corporation Gel composition containing carbonaceous compound
US5885335A (en) * 1996-06-14 1999-03-23 Cabot Corporation Modified carbon products and inks and coatings containing modified carbon products
US5895522A (en) * 1997-08-12 1999-04-20 Cabot Corporation Modified carbon products with leaving groups and inks and coatings containing modified carbon products
WO1999031175A1 (en) * 1997-12-15 1999-06-24 Cabot Corporation Polymeric products containing modified carbon products and methods of making and using the same
US5922118A (en) * 1996-06-14 1999-07-13 Cabot Corporation Modified colored pigments and ink jet inks, inks, and coatings containing modified colored pigments
US6068688A (en) * 1997-11-12 2000-05-30 Cabot Corporation Particle having an attached stable free radical and methods of making the same
US6069190A (en) * 1996-06-14 2000-05-30 Cabot Corporation Ink compositions having improved latency
US6103380A (en) * 1998-06-03 2000-08-15 Cabot Corporation Particle having an attached halide group and methods of making the same
US6337358B1 (en) 1997-10-31 2002-01-08 Cabot Corporation Particles having an attached stable free radical, polymerized modified particles, and methods of making the same
US6368239B1 (en) 1998-06-03 2002-04-09 Cabot Corporation Methods of making a particle having an attached stable free radical
US6387500B1 (en) 1997-11-06 2002-05-14 Cabot Corporation Multi-layered coatings and coated paper and paperboards
US6472471B2 (en) 1997-12-16 2002-10-29 Cabot Corporation Polymeric products containing modified carbon products and methods of making and using the same
WO2004018569A1 (en) * 2000-12-08 2004-03-04 Columbian Chemicals Company Method for producing additive carbon black

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ZA933185B (en) * 1992-05-08 1994-05-23 Dick Co Ab Encapsulated magnetic particles pigments and carbon black compositions and methods related thereto
US5869550A (en) 1995-05-22 1999-02-09 Cabot Corporation Method to improve traction using silicon-treated carbon blacks
JP3977437B2 (en) 1996-09-25 2007-09-19 キャボット コーポレイション Silicon-treated carbon black pretreated with a coupling agent
US6197274B1 (en) 1996-09-25 2001-03-06 Cabot Corporation Silica coated carbon blacks
US6017980A (en) 1997-03-27 2000-01-25 Cabot Corporation Elastomeric compounds incorporating metal-treated carbon blacks
US5904762A (en) 1997-04-18 1999-05-18 Cabot Corporation Method of making a multi-phase aggregate using a multi-stage process
US6051060A (en) * 1997-12-04 2000-04-18 Marconi Data Systems, Inc. Method of making pigment with increased hydrophilic properties
SG129313A1 (en) * 2005-07-27 2007-02-26 Denka Singapore Private Ltd Carbon black, method for producing the same, and its use
AT514774B1 (en) * 2013-08-30 2016-08-15 Avl List Gmbh Equipment for a condensation nucleus counter for combustion engine exhaust gases
WO2021223789A1 (en) 2020-05-05 2021-11-11 Suncoal Industries Gmbh Biogenic black pigment, method for the production thereof and use thereof
EP4334396A1 (en) 2021-05-05 2024-03-13 SunCoal Industries GmbH Biogenic black pigment, method for the production thereof and use thereof

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB721467A (en) * 1952-01-21 1955-01-05 David Child Soul Improvements in or relating to coated solid particles
GB952855A (en) * 1959-06-11 1964-03-18 Hoechst Ag Process for the manufacture of non-dusty pulverulent substances
GB1103858A (en) * 1964-06-04 1968-02-21 Huels Chemische Werke Ag Process for impregnating fillers
GB1128706A (en) * 1966-03-29 1968-10-02 Monsanto Co Antidegradant compositions
GB1241187A (en) * 1966-09-12 1971-07-28 Kores Mfg Company Ltd Improvements in the production of copy sheets
GB1325371A (en) * 1970-05-14 1973-08-01 Koege Kemisk Vaerk Pre-treated pigments
GB1518777A (en) * 1976-03-27 1978-07-26 Hoechst Ag Process for imparting antistatic properties to rubber
GB1537379A (en) * 1975-05-05 1978-12-29 Cabot Corp Carbon black compositions and black-pigmented compositions containing same

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1848213A (en) * 1929-09-07 1932-03-08 Wiegand William Bryan High color carbon black
US2867540A (en) * 1955-12-30 1959-01-06 Monsanto Chemicals Modified carbon black product and process
FR1331889A (en) * 1962-08-24 1963-07-05 Bayer Ag Manufacture of carbon black preparations
US3340081A (en) * 1963-12-26 1967-09-05 Phillips Petroleum Co Treatment of carbon black
US3338729A (en) * 1964-05-26 1967-08-29 Phillips Petroleum Co Oil impregnation of carbon black
DE1767950A1 (en) * 1968-07-04 1971-09-30 Henkel & Cie Gmbh Process for hydrophobing carbon black
DE1769728A1 (en) * 1968-07-04 1971-10-28 Henkel & Cie Gmbh Hydrophobic carbon black in rubber compounds
US4001035A (en) * 1974-01-16 1977-01-04 Dainichiseika Color & Chemicals Mfg. Co., Ltd. Coloring composition

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB721467A (en) * 1952-01-21 1955-01-05 David Child Soul Improvements in or relating to coated solid particles
GB952855A (en) * 1959-06-11 1964-03-18 Hoechst Ag Process for the manufacture of non-dusty pulverulent substances
GB1103858A (en) * 1964-06-04 1968-02-21 Huels Chemische Werke Ag Process for impregnating fillers
GB1128706A (en) * 1966-03-29 1968-10-02 Monsanto Co Antidegradant compositions
GB1241187A (en) * 1966-09-12 1971-07-28 Kores Mfg Company Ltd Improvements in the production of copy sheets
GB1325371A (en) * 1970-05-14 1973-08-01 Koege Kemisk Vaerk Pre-treated pigments
GB1537379A (en) * 1975-05-05 1978-12-29 Cabot Corp Carbon black compositions and black-pigmented compositions containing same
GB1518777A (en) * 1976-03-27 1978-07-26 Hoechst Ag Process for imparting antistatic properties to rubber

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996018456A2 (en) * 1994-12-15 1996-06-20 Cabot Corporation Gel composition containing carbonaceous compound
WO1996018456A3 (en) * 1994-12-15 1996-08-29 Cabot Corp Gel composition containing carbonaceous compound
US6110994A (en) * 1996-06-14 2000-08-29 Cabot Corporation Polymeric products containing modified carbon products and methods of making and using the same
US5885335A (en) * 1996-06-14 1999-03-23 Cabot Corporation Modified carbon products and inks and coatings containing modified carbon products
US5922118A (en) * 1996-06-14 1999-07-13 Cabot Corporation Modified colored pigments and ink jet inks, inks, and coatings containing modified colored pigments
US6069190A (en) * 1996-06-14 2000-05-30 Cabot Corporation Ink compositions having improved latency
US5968243A (en) * 1997-08-12 1999-10-19 Belmont; James A. Modified carbon products with leaving groups inks and coatings containing modified carbon products
US5895522A (en) * 1997-08-12 1999-04-20 Cabot Corporation Modified carbon products with leaving groups and inks and coatings containing modified carbon products
US6337358B1 (en) 1997-10-31 2002-01-08 Cabot Corporation Particles having an attached stable free radical, polymerized modified particles, and methods of making the same
US6387500B1 (en) 1997-11-06 2002-05-14 Cabot Corporation Multi-layered coatings and coated paper and paperboards
US6068688A (en) * 1997-11-12 2000-05-30 Cabot Corporation Particle having an attached stable free radical and methods of making the same
WO1999031175A1 (en) * 1997-12-15 1999-06-24 Cabot Corporation Polymeric products containing modified carbon products and methods of making and using the same
US6472471B2 (en) 1997-12-16 2002-10-29 Cabot Corporation Polymeric products containing modified carbon products and methods of making and using the same
US6103380A (en) * 1998-06-03 2000-08-15 Cabot Corporation Particle having an attached halide group and methods of making the same
US6350519B1 (en) 1998-06-03 2002-02-26 Cabot Corporation Particle having an attached halide group and methods of making the same
US6368239B1 (en) 1998-06-03 2002-04-09 Cabot Corporation Methods of making a particle having an attached stable free radical
US6551393B2 (en) 1998-06-03 2003-04-22 Cabot Corporation Methods of making a particle having an attached stable free radical
US6664312B2 (en) 1998-06-03 2003-12-16 Cabot Corporation Particle having an attached halide group and methods of making the same
US7282526B2 (en) 1998-06-03 2007-10-16 Cabot Corporation Particle having an attached halide group and methods of making the same
WO2004018569A1 (en) * 2000-12-08 2004-03-04 Columbian Chemicals Company Method for producing additive carbon black

Also Published As

Publication number Publication date
ZA87118B (en) 1987-08-26
IN168779B (en) 1991-06-01
LU86811A1 (en) 1987-08-12
DD258996A5 (en) 1988-08-10
CZ186987A3 (en) 1996-04-17
AU7050287A (en) 1987-10-01
SE465464B (en) 1991-09-16
JPS62275164A (en) 1987-11-30
HU200613B (en) 1990-07-28
KR870008975A (en) 1987-10-22
KR950006688B1 (en) 1995-06-21
DK147287D0 (en) 1987-03-23
IL81236A (en) 1991-06-30
ES2004891A6 (en) 1989-02-16
GB8705181D0 (en) 1987-04-08
CN87102344A (en) 1987-10-14
YU226286A (en) 1988-02-29
FR2596055A1 (en) 1987-09-25
PT84488A (en) 1987-04-01
GB2188311B (en) 1990-10-24
IT1203367B (en) 1989-02-15
MX168266B (en) 1993-05-14
CN1025863C (en) 1994-09-07
CZ281256B6 (en) 1996-07-17
IT8719717A0 (en) 1987-03-16
JPH0125785B2 (en) 1989-05-19
AR245760A1 (en) 1994-02-28
DK147287A (en) 1987-09-25
IL81236A0 (en) 1987-08-31
FR2596055B1 (en) 1989-09-15
PL264782A1 (en) 1988-02-04
BE906089A (en) 1987-04-16
SE8700311L (en) 1987-09-25
YU44613B (en) 1990-10-31
PT84488B (en) 1989-11-10
PL152526B1 (en) 1991-01-31
BR8701003A (en) 1987-12-29
NL8700664A (en) 1987-10-16
HUT46718A (en) 1988-11-28
SE8700311D0 (en) 1987-01-27
DE3703077A1 (en) 1987-10-01
AU599087B2 (en) 1990-07-12
NZ219110A (en) 1990-04-26

Similar Documents

Publication Publication Date Title
GB2188311A (en) Process for modifying the surface characteristics of carbon black
Narkis et al. Electrical properties of carbon black filled crosslinked polyethylene
EP0081004B1 (en) Organic matrix composites reinforced with intercalated graphite
US4702860A (en) Current-conducting composition
US4107092A (en) Novel compositions of matter
CA1073582A (en) Process for imparting antistatic properties to plastics
CA1057948A (en) Conductive polyolefin compositions
US3764376A (en) Antistatic resinous compositions
Aminabhavi et al. Electrical resistivity of carbon-black-loaded rubbers
US2761849A (en) Conductive plastic product
US4175152A (en) Polymeric materials containing semiconducting refractory oxides
US2959563A (en) Resinous 1-monoolefinic hydrocarbon compositions stabilized with silicon monoxide
Kraus et al. Electrical Conductivity of Carbon Black‐Reinforced Elastomers
JP7465811B2 (en) Composites of non-polar organic polymers and ultra-low wettability carbon blacks
DE2834390C2 (en) Electrically conductive plastic molding compound for adjustable resistors and process for their production
Sommers Carbon black for electrically conductive plastics
DE2120197A1 (en) Semiconducting polymer compositions and their use
JPS6365226B2 (en)
RU2815021C1 (en) Antistatic composition of substances for applying coatings on surface of fiberglass articles
RU2083619C1 (en) Conducting paint and varnish material
US5985194A (en) Method of making polymeric semiconductor body
CA1039436A (en) Dielectric polyolefin compositions
STEIN Polyethylene zyxwvutsrqponmlkj
JPH01101372A (en) Electrically conductive composite resin composition
CA2067721C (en) Conductive polymer compositions

Legal Events

Date Code Title Description
PCNP Patent ceased through non-payment of renewal fee

Effective date: 19940305