CA2258189A1 - Modified carbon adsorbents and processes for adsorption using the same - Google Patents

Modified carbon adsorbents and processes for adsorption using the same Download PDF

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CA2258189A1
CA2258189A1 CA002258189A CA2258189A CA2258189A1 CA 2258189 A1 CA2258189 A1 CA 2258189A1 CA 002258189 A CA002258189 A CA 002258189A CA 2258189 A CA2258189 A CA 2258189A CA 2258189 A1 CA2258189 A1 CA 2258189A1
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carbonaceous material
adsorbate
organic group
adsorption
group
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CA002258189A
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French (fr)
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Ranjan Ghosal
James A. Belmont
Douglas M. Smith
Jameel Menashi
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Cabot Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J41/00Anion exchange; Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/08Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/18Carbon, coal or tar
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J39/00Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
    • B01J39/08Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
    • B01J39/24Carbon, coal or tar

Abstract

An adsorbant composition containing a modified carbonaceous material capable of adsorbing an adsorbate is disclosed, wherein at least one organic group is attached to the carbonaceous material. Furthermore, methods to increase the adsorption capacity of a carbonaceous material capable of adsorbing an adsorbate and methods to adsorb an adsorbate using the above-described adsorbant composition are also disclosed.

Description

CA 022~8189 1998-12-14 MODIFIED CARBON ADSORBENTS AND PROCESSES FOR
ADSORPTION USING THE SAME

FIELD OF THE INVENTION
This invention relates to carbon adso~b~ made from modified carbonaceous materials and also relates to a method of using these adsoll,cl,L~, including a method to increase the adsorption capacity and/or alter the adsorption affinity of ca-l~onaeeous materials capable of ads~,ll,ing an adsorbate.
BACKGROUND OF THE INVENTION
Adsorption is an important operation in many industrial proeesses. The effectiveness of an adsorbent depends, primarily, on its surface area, pore structure, and surface ch~ try. The nature of the adsorbate whieh is to be adsorbed frequently dictates the ch~omic~l nature of the adsorbent. For exarnple, carbonaceous adso~ are often used to selectively remove organic compounds from liquid, gaseous, or vapor media. Silica and alumina based adsorbents are employed to selectively adsorb polar adsorbates sueh as water, ammonia, and the like from similar media.
The efficacy of an adsorbent for a particular applieation is usually ~let~rminPd by the adsorption capacity and selectivity of the adsorbent for the adsorbate in question. The adsorption capacity may be measured per unit mass or per unit volume of the adsorbent. In general, the higher the adsorption eapacity and selectivity of an adsorbent for a particular adsorbate, the more useful it is, since less of the adsorbent has to be used to effect the same removal of the adsorbate.
Carbonaceous materials, such as activated earbon, earbon black, and the like, represent an important class of adsorbents which are used in many fields sueh as separation, purification, and waste among others. Because of their widespread use, any method for improving the adsorption properties of carbonaceous adsorbents for a particular adsorbate can have a large impact on the effieacy and economy of the proeesses utilizing them. Therefore, attempts have been made in the past to modify the surfaee che~ y of earbonaeeous adsorbents. The methods employed for their modification can be broadly classified into physical and rh~mi~l means. In surface modif~ ion by physical means, a speeies is deposited on the surface of the carbonaceous adsorbent to form a layer which then changes its SUBSTITUTE SHE~T (~ULE 26) , . .. . . . .

CA 022~8189 1998-12-14 W O 97/47382 PCTrUS97/08859 adsorption properties. However, such modification teçhniques have limited utility because the deposited layer is easily removed. In surface modification by ~-.h.omir~l means, the modifying species is attached to the carbon surface by a chemical bonding m.orh~ni~m The characteristics of the adsorption isotherm, representing the relationship between the extent 5 of adsorption and adsorbate concentration or adsorbate partial pressure at a fixed temperature, is also of importance. As described by Sircar et al. in "Activated Carbon for Gas Separation and Storage,"
Carbon, Vol. 34, No. 1, pp. 1-12 (1996), the characteristics of the preferred adsorption isotherm will depend on the separation process being employed For example, in cases where adsorbent regeneration is effected by a ~les~ule swing, the preferred adsorbent is one with a moderate affinity for the adsorbate.
10 When the adsorbate is strongly adsorbed, that is, when it has a strong affinity for the adsorbent, regeneration becomes difficult and energy intensive. On the other hand, when the adsorbent exhibits a weak affinity for the adsorbate, it has a small adsorption capacity at low adsorbent partial plcS~ul~S and, hence, the adsorption mass transfer zone becomes very long. Thus, the availability of a method for altering the affinity of an adsorbent for an adsorbate is advantageous.
Thus, any method for increasing the adsorption capacity and/or modifying the adsorption affinity of the adsorbent enh~nres its usefulness in adsorption applications. As already noted, chemical modification can be used to alter the adsorptive properties of carbonaceous adsorbents. The range of chemical species which can be attached, however, is limited.
Bansal, Donnet and Stoeckli (in Chapter 5 of Active Carbon, Marcel Dekker, Inc., 1988) have reviewed dirrele--~ techniques of carbon surface modification. Physical hll~ lla~ion methods are described, as are methods that rely on chemical reactions with various species to modify the surface of the carbon. Some of the chemical surface modification techniques described by Bansal et al. are oxidation, halogenation, sulfonation, and ammoniation. Several of these techniques require treatment of the carbon at elevated temperatures. Another technique involving oxidation of the carbon with HNO3 in the presence of a catalyst, has been described by Sircar and Golden (U.S. Patent No. 4,702,749).
However, these techniques have certain disadvantages appa~ to those familiar with the field.

SUBSTITUTE SHE~T (RUL~ 26) CA 022~8189 1998-12-14 W O 97/47382 PCT~US97/088S9 In view of the limited utility of rhPmi~l means of modifying the surfaces of carbonaceous adsorbents, there still is a need to develop mo-lifiPd carbon adsorbents, plcfel~ly with improved adsorption capacity over the unmodified material.
SUMMARY OF THE INVENTION
To achieve these and other advantages and in accordance with the purposes of the present invention, as embodied and broadly described herein, the present invention relates to an adsorbent composition containing a modified call,ollace~ ~IS material capable of adsorbing an adsorbate.
Another embodiment of the present invention relates to a method to increase the adsorption capacity of a carbonaceous material capable of adsorbing an adsorbate or altering the adsorption isotherm of the adsorbate on the adsorbent, for instance, to allow an easier r~g~ lalion of the adsorbent. In this method, at least one organic group capable of increasing the adsorption capacity of a carbonaceous material is attached to the carbonaceous material.
The present invention, in addition, relates to a method of adsorbing an adsorbate and includes the step of cont~rting the adsorbate with a carbonaceous material which has been mo~lified by ~tt~hing an organic group. The modified carbonaceous material is capable of adsorbing the adsorbate and at least one organic group is attached to the carbonaceous material.
Additional features and advantages of the present invention will be set forth in part in the description which follows, and in part will be d~ale.,L from the description, or may be learned by practice of the present invention. The objectives and other advantages of the present invention will be realized and attained by means of the elPnnPnt.c and combinations particularly pointed out in the written description and appended claims.
It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are intended to provide further explanation of the present invention, as claimed.
The acc~,l,lpallyhlg figures, which are incorporated in and constitute a part of this specification, illustrate several embodiments of the present invention and together with the description, serve to explain the principles of the present invention.
SUBSTITUTE SI~EET (RULE 26) CA 022~8189 1998-12-14 W O 97/47382 PCT~US97/08859 BRIEF DESCRIPrION OF THE DRAWINGS
Figure 1 is a graph plotting the amount of water adsorption on modified and unmodified carbon black.
Figure 2 is a graph plotting the amount of water adsorption on modified and umnodified activated 5 carbon.
Figure 3 is a graph plotting the amount of water adsorption on modified and unmodified carbon black per unit surface area.
Figure 4 is a graph plotting the amount of water adsorption on modified and unmodified activated carbon per unit surface area.
Figure 5 is a graph plotting the amount of CO2 adsorption on modified and unmodified carbon black at 273 K.
DETAILED DESCRIPTION OF THE PRESENT INVENTION
In further detail, an adsorbent composition of the present invention contains a modified carbonaceous material capable of adsorbing an adsorbate wherein at least one organic group is attached 15 to the carbonaceous material.
The carbonaceous material capable of adsorbing an adsorbate includes, but is not limited to, activated carbon, carbon black, or other carbonaceous material obtained by the pyrolysis of cellulosic, fuel oil, polymeric, or other precursors. This includes carbonaceous material which is a waste product or by-product. Preferably, the carbonaceous material is activated carbon or carbon black capable of 20 adsorbing an adsorbate. Comrnercial examples of carbon black include, but are not limited to, Black Pearls7 2000 carbon black, Black Pearls7 430 carbon black, Black Pearls7 900 carbon black, and Black Pearls7 120 carbon black, all available from Cabot Corporation. Commercial examples of activated carbon include Darco SS1, available from Norit; Sorbonorit 3, available from Norit; and BPL activated carbon from Calgon. The carbonaceous material modified by 25 the procedures described herein may be a microporous or mesoporous activated carbon in granular or pellet form; a carbon black of different structures in fluffy or pelleted form; or any other carbonaceous material whose applicability to this invention is apparent to those skilled SUBSTITUTE SWEET !RULE 26) CA 022~8189 1998-12-14 W 097/47382 PCTrUS97/08859 in the art, such as carbon fibers or carbon cloth. The choice of carbonaceous material used eventually depends on a variety of different factors, including the application for which it is int~.ntle~l Each of these types of carbonaceous material has the ability to adsorb at least one adsorbate. A variety of BET surface areas, micropore volumes, and total pore volumes are S available depending on the desired end use of the carbonaceous material.
Carbonaceous materials include, but are not limited to, material obtained by the compaction of small carbon particles and other finely divided forms of carbon as long as the carbon has the ability to adsorb at least one adsorbate and is capable of being chemically modified in accordance with the present invention.
The carbonaceous material described above is then modified by the ~ c.hment of an organic group to the carbonaceous material. Preferred processes for attaching an organic group to a carbonaceous material are described in detail in U.S. Patent Application Nos. 08/356,660, 08/572,525, 08/356,459, and 08/356,653, all incorporated in their entirety by reference herein. These processes can be preferably used in p~ g the modified carbon 15 adsorbents of the present invention and permit the attachment of an organic group to the carbonaceous material via a chemical reaction. As indicated above, the organic group attached to the carbonaceous material is one preferably capable of increasing the adsorption capacity of the carbonaceous material.
A prcf~ ed process for ;qtt:~r.hing an organic group to the carbonaceous materials 20 involves the reaction of at least one diazonium salt with a carbonaceous material in the ~bsçn~e of an externally applied current sufficient to reduce the diazonium salt. That is, the reaction between the diazonium salt and the carbonaceous material proceeds without an external source of electrons sufficient to reduce the diazoniurn salt. Mixtures of dirr~l~nt diazonium salts may be used. This process can be carried out under a variety of reaction SUBSTITUTE S~ET (RULE 26) CA 022~8189 1998-12-14 W 097/47382 PCT~US97/08859 --6--conditions and in any type of reaction medium, including both protic and aprotic solvent systems or slurries.
In another preferred process, at least one diazoniulll salt reacts with a carbonaceous material in a protic reaction medium. Mixtures of dirre~elll diazonium salts may be used in S this process. This process can also be carried out under a variety of reaction conditions.
Preferably, in both processes, the diazonium salt is formed in situ. If desired, in either process, the modified carbonaceous material can be isolated and dried by means known in the art. Furthermore, the modified carbonaceous material can be treated to remove impurities by known techniques. The various preferred embodiments of these processes are discussed 10 below.
The processes can be carried out under a wide variety of conditions and in general are not limited by any particular condition. The reaction conditions must be such that the particular diazonium salt is sufficiently stable to allow it to react with the carbonaceous material. Thus, the processes can be carried out under reaction conditions where the 15 diazoniurn salt is short lived. The reaction between the diazonium salt and the carbonaceous material occurs, for example, over a wide range of pH and temperature. The processes can be carried out at acidic, neutral, and basic pH. Preferably, the pH ranges from about 1 to 9.
The reaction temperature may preferably range from 0OC to 100~C.
Diazonium salts, as known in the art, may be formed for example by the reaction of 20 primary amines with aqueous solutions of nitrous acid. A general discussion of diazonium salts and methods for their ~lepat~lion is found in Morrison and Boyd, Or~anic ChemistrY, 5th Ed., pp. 973-983, (Allyn and Bacon, Inc. 1987) and March, Advanced Or~anic ChemistrY:
Reactions. Meçh~ni~m~l and Structures, 4th Ed., (Wiley, 1992). According to this invention, a diazonium salt is an organic compound having one or more diazonium groups.

SUBSTITUTE SHEET (RULE 26) CA 022~8189 1998-12-14 W O 97/47382 PCT~US97/08859 The diazonium salt may be ~ a,ed prior to reaction with the carbonaceous material or, more preferably, generated in situ using techniques known in the art. In situ generation ~ also allows the use of unstable diazonium salts such as alkyl diazonium salts and avoids llnnecess~ry h~n(lling or manipulation of the diazonium salt. In particularly preferred S processes, both the nitrous acid and the diazoniuln salt are generated in situ.
A diazonium salt, as is known in the art, may be generated by reacting a primaryamine, a nitrite and an acid. The nitrite may be any metal nitrite, preferably lithium nitrite, sodium nitrite, potassium nitrite, or zinc nitrite, or any organic nitrite such as for example isoamylnitrite or ethylnitrite. The acid may be any acid, inorganic or organic, which is effective in the generation of the diazonium salt. Preferred acids include nitric acid, HNO3, hydrochloric acid, HCI, and sulfuric acid, H2S04.
The diazonium salt may also be generated by reacting the primary amine with an aqueous solution of nitrogen dioxide. The aqueous solution of nitrogen dioxide, NO2/H2O, provides the nitrous acid needed to generate the diazonium salt.
Generating the diazonium salt in the presence of excess HCI may be less preferred than other alternatives because HCI is corrosive to stainless steel. Generation of the diazonium salt with NO2/H2O has the additional advantage of being less corrosive to stainless steel or other metals commonly used for reaction vessels. Generation using H2SO4/NaNO2 or HNO3/NaNO2 are also relatively non-corrosive.
In general, generating a diazonium salt from a primary amine, a nitrite, and an acid requires two equivalents of acid based on the amount of amine used. In an in situ process, the diazonium salt can be generated using one equivalent of the acid. When the primary - amine contains a strong acid group, adding a separate acid may not be necessary. The acid group or groups of the primary amine can supply one or both of the needed equivalents of acid. When the primary amine contains a strong acid group, preferably either no additional SUBSTITUTE SHEET tRULE 26) .

CA 022~8189 1998-12-14 W O 97/47382 PCT~US97/08859 acid or up to one equivalent of additional acid is addtd to a process of the invention to generate the diazonium salt in situ. A slight excess of additional acid may be used. One example of such a primary amine is para-aminobenzenesulfonic acid (sl-lfanilic acid).
In general, di~onium salts are thermally unstable. They are typically prepared in 5 solution at low temperatures, such as 0-5~C, and used without isolation of the salt. Heating solutions of some diazonium salts may liberate nitrogen and form either the corresponding alcohols in acidic media or the organic free radicals in basic media.
However, the diazonium salt need only be sufficiently stable to allow reaction with the carbonaceous material. Thus, the processes can be carried out with some diazo~ .l salts 10 otherwise considered to be unstable and subject to decomposition. Some decomposition processes may compete with the reaction between the carbonaceous material and the diazonium salt and may reduce the total number of organic groups attached to the carbonaceous material. Further, the reaction may be carried out at elevated temperatures where many diazonium salts may be susceptible to decomposition. Elevated temperatures may 15 also advantageously increase the solubility of the diazonium salt in the reaction medium and improve its h~n~ling during the process. However, elevated temperatures may result in some loss of the diazonium salt due to other decomposition processes.
Reagents can be added to form the diazonium salt in situ, to a suspension of carbonaceous material in the reaction medium, for example, water. Thus, a carbonaceous 20 material suspension to be used may already contain one or more reagents to generate the diazonium salt and the process accomplished by adding the rem~ining reagents.
Reactions to form a diazonium salt are compatible with a large variety of functional groups commonly found on organic compounds. Thus, only the availability of a diazonium salt for reaction with a carbonaceous material limits the processes of the invention.

SUBSTITUTE SI~EET (RULE 26) CA 022~8189 1998-12-14 W O 97/47382 PCTrUS97/08859 The processes can be carried out in any reaction medium which allows the reaction between the diazonium salt and the carbonaceous material to proceed. Preferably, the reaction medium is a solvent-based system. The solvent may be a protic solvent, an aprotic solvent, or a mixture of solvents. Protic solvents are solvents, like water or methanol, cur~ g a 5 hydrogen a~t~rhed to an oxygen or nitrogen and thus are sufficiently acidic to form hydrogen bonds. Aprotic solvents are solvents which do not contain an acidic hydrogen as defined above. Aprotic solvents include, for example, solvents such as hex~nes, tetrahydrofuran (THF), acetonitrile, and berl70nitrile. For a discussion of protic and aprotic solvents see Morrison and Boyd, Or~anic Chemistrv, 5th Ed., pp. 228-231, (Allyn and Bacon, Inc. 1987).
The processes are preferably carried out in a protic reaction medium, that is, in a protic solvent alone or a mixture of solvents which contains at least one protic solvent. Preferred protic media include, but are not limited to water, aqueous media cont:lining water and other solvents, alcohols, and any media cont~ining an alcohol, or mixtures of such media.
The reaction between a diaGu~ salt and a carbonaceous material can take place with 15 any type of carbonaceous material, for example, in finely divided state or pelleted form. In one embodiment designed to reduce production costs, the reaction occurs during a process for forming carbonaceous material pellets. For example, a carbonaceous material product of the invention can be prepared in a dry drum by spraying a solution or slurry of a diazonium salt onto a carbonaceous material. Alternatively, the carbonaceous material product can be 20 prepared by pelletizing a carbonaceous material in the presence of a solvent system, such as water, co~ g the diazonium salt or the reagents to generate the diazonium salt in situ.
Aqueous solvent systems are preferred. In general, the processes produce inorganic by-products, such as salts. In some end uses, such as those discussed below, these by-products may be undesirable. Several possible ways to produce a carbonaceous material product 25 without unwanted inorganic by-products or salts are as follows:
SUBSTITUTE S~EET (RULE 26) CA 022~8189 1998-12-14 W 097/47382 PCT~US97/08859 First, the diazonium salt can be purified before use by removing the unwanted inorganic by-product using means kno~vn in the art. Second, the diazonium salt can be generated with the use of an organic nitrite as the diazotization agent yielding the corresponding alcohol rather than an inorganic salt. Third, when the diazonium salt is 5 generated from an amine having an acid group and aqueous NO2, no inorganic salts are formed. Other ways may be known to those of skill in the art.
In addition to the inorganic by-products, the process may also produce organic by-products. They can be removed, for example, by extraction with organic solvents. Other ways of obtaining products without unwarranted organic by-products may be known to those 10 of skill in the art, and include washing or removal of ions by reverse osmosis.
The reaction between a diazonium salt and a carbonaceous material forms a carbonaceous material product having an organic group attached to the carbonaceous material.
The diazonium salt may contain the organic group to be attached to the carbonaceous material.
It may be possible to produce the carbonaceous material products of this invention by other 15 means known to those skilled in the art.
The organic group may be an aliphatic group, a cyclic organic group, or an organic compound having an aliphatic portion and a cyclic portion. As discussed above, the diazonium salt employed can be derived from a primary amine having one of these groups and being capable of forming, even transiently, a diazonium salt. The organic group may be 20 substituted or unsubstituted, branched or unbranched. Aliphatic groups include, for example, groups derived from alkanes, alkenes, alcohols, ethers, aldehydes, ketones, carboxylic acids, and carbohydrates. Cyclic organic groups include, but are not limited to, alicyclic hydrocarbon groups (for example, cycloalkyls, cycloalkenyls), heterocyclic hydrocarbon groups (for example, pyrrolidinyl, pyrrolinyl, piperidinyl, morpholinyl, and the like), aryl groups (for 25 example, phenyl, naphthyl, anthracenyl, and the like), and heteroaryl groups (imidazolyl, ~UB~TITUTE SHEET (F~ULE 26) CA 022~8189 1998-12-14 W O 97147382 PCT~US97/08859 pyra_olyl, pyridinyl, thienyl, thiazolyl, furyl, indolyl, and the like). As the steric hinderance of a substituted organic group increases, the number of organic groups att~h~-i to the carbonaceous material from the reaction bet~,veen the diaGonium salt and the carbonaceous material may be ~limini~he~l When the organic group is substituted, it may contain any functional group compatible with the formation of a diazonium salt. Functional groups include, but are not limited to, R, OR, COR, COOR, OCOR, carboxylate salts such as COOLi, COONa, COOK, COO-NR4+, halogen, CN, NR2, S03H, sulfonate salts such as SO3Li, SO3Na, SO3K, SO3-NR4~, OSO3H, OSO3- salts, NR(COR), CONR2, NO2, PO3H2, phosphonate salts such as PO3HNa and PO3Na2, phosphate salts such as OPO3HNa and OPO3Na2, N=NR, NR3+X-, PR3~X-, SkR, SSO3H, SSO3-salts, SO2NRR', S02SR, SNRR', SNQ, SO2NQ, CO2NQ, S-(1,4-pipt;~ ediyl)-SR, 2-(1,3-dithianyl) 2-(1,3-dithiolanyl), SOR, and SO2R. R and R', which can be the same or .lirr~,le~
are indepf n~iently hydrogen, branched or unbranched C,-C20 substituted or unsubstituted, saturated or unsaturated hydrocarbon, e.g., alkyl, alkenyl, alkynyl, substituted or unsubsliluled aryl, substituted or unsubstituted heteroaryl, ~ub~liluled or unsubstituted alkylaryl, or substituted or unsubstituted arylalkyl. The integer k ranges from 1-8 and preferably from 2-4.
The anion X- is a halide or an anion derived from a mineral or organic acid. Q is (CH2)W, (CH2)xO(CH2)~, (CH2)xNR(CH2)z, or (CH2)xS(CH2)z, where w is an integer from 2 to 6 and x and z are integers from 1 to 6. In the above formula, specific examples of R and R' are NH2-C6H4-, CH2CH2-C6H4-NH2, CH2-C6H4-NH2, and C6Hs.
Another example of an organic group is an aromatic group of the formula AyAr-, which corresponds to a primary arnine of the formula AyArNH2. In this formula, the variables have the following m~ning~ Ar is an aromatic radical such as an aryl or heteroaryl group. Ar can be selected from the group con~ ting of phenyl, naphthyl, anthracenyl, phen~..lh-enyl,~5 biphenyl, pyridinyl, benzothi~ 701yl, and ben_othia_olyl; A is a substituent on the aromatic SUBSTITUTE S'IEET (RULE 26) CA 022~8189 1998-12-14 radical independently selected from a preferred functional group described above or A is a linear, branched or cyclic hydrocarbon radical (preferably containing 1 to 20 carbon atoms), unsubstituted or substituted with one or more of those functional groups; and y is an integer from 1 to the total nurnber of -CH radicals in the aromatic radical. For instance, y is an integer from 1 to 5 when Ar is phenyl, 1 to 7 when Ar is naphthyl, 1 to 9 when Ar is anthracenyl, phenanthrenyl, or biphenyl, or 1 to 4 when Ar is pyridinyl.
Another set of organic groups which may be attached to the carbonaceous material are organic groups substituted with an ionic or an ionizable group as a functional group. An ionizable group is one which is capable of forming an ionic group in the medium of use. The ionic group may be an anionic group or a cationic group and the ionizable group may form an anion or a cation.
Ionizable functional groups forming anions include, for example, acidic groups or salts of acidic groups. The organic groups, therefore, include groups derived from'organic acids.
Preferably, when it contains an ionizable group forming an anion, such an organic group has a) an aromatic group or a C,-C~2 alkyl group and b) at least one acidic group having a pKa of less than 11, or at least one salt of an acidic group having a pKa of less than 11, or a mixture of at least one acidic group having a pKa of less than 11 and at least one salt of an acidic group having a pKa of less than 11. The pKa of the acidic group refers to the pKa of the organic group as a whole, not just the acidic substituent. More preferably, the pKa is less than 10 and most preferably less than 9. Preferably, the aromatic group or the C~-CI2 alkyl group of the organic group is directly attached to the carbonaceous material. The aromatic group may be further substituted or unsubstituted, for example, with alkyl groups. The organic group can be a phenyl or a naphthyl group and the acidic group is a sulfonic acid group, a sulfinic acid group, a phosphonic acid group, or a carboxylic acid group. Examples of these acidic groups and their salts are discussed above. The organic group can be a SUBSTITUTE SHEET (F~ULE 26) CA 022~8189 1998-12-14 W 097/47382 PCTrUS97/08859 substituted or unsubstituted sulfophenyl group or a salt thereof; a substituted or unsubstituted (polysulfo)phenyl group or a salt thereof; a substituted or unsubstituted sulfonaphthyl group - or a salt thereof; or a ~ubsliluled or unsubstituted (polysulfo)naphthyl group or a salt thereof.
An example of a sub~lilul~d sulfophenyl group is hydroxysulfophenyl group or a salt thereof.
Specific organic groups having an ionizable functional group forming an anion (and their corresponding primary arnines for use in a process according to the invention) are p-sulfophenyl (p-sulfanilic acid), 4-hydroxy-3-sulfophenyl (2-hydroxy-5-amino-benzenesulfonic acid), and 2-sulfoethyl (2-arninoeth~neslllfonic acid).
Amines re~lesellt examples of ionizable functional groups that form cationic groups.
10 For example, amines may be protonated to form ammonium groups in acidic media.
Preferably, an organic group having an amine substituent has a pKb of less than 5.
Quaternary ammonium groups (-NR3+) and quaternary phosphonium groups (-PR3+) also esen~ examples of cationic groups. The organic group can contain an aromatic group such as a phenyl or a naphthyl group and a ql~tern~ry ammonium or a quaternary phosphonium 15 group. The aromatic group is preferably directly attached to the carbonaceous material.
Q~tPrni7~d cyclic amines, and even quaternized aromatic arnines, can also be used as the organic group. Thus, N-substituted pyridinium compounds, such as N-methyl-pyridyl, can be used in this regard. Examples of organic groups include, but are not limited to, (C5H4N)C2H5+X-, C6H4(NC5H5)+X-, C6H4COCH2N(CH3)3 X-, C6H4COCH2(NC5H5) X, (C5H4N)CH3+X-, and C6H4CH2N(CH3)3+X-, where X~ is a halide or an anion derived from a mineral or organic acid .
Aromatic sulfides encompass another group of organic groups. These aromatic sulfides can be represented by the formulas Ar(CH2)qSk(CH2)rAr' or A-(CH2)qSK(CH2)rAr" wherein Ar and Ar' are independently substituted or lln~llbstituted arylene or heteroarylene groups, Ar"
is an aryl or heteroaryl group, k is 1 to 8 and q and r are 0-4. Substituted aryl groups would SUBSTITUTE Sl IEET (RULE 26) CA 022~8l89 l998-l2-l4 include substituted alky}aryl groups. Examples of arylene groups include phenylene groups, particularly p-phenylene groups, or benzothiazolylene groups. Aryl groups include phenyl, naphthyl and benzothiazolyl. The number of sulfurs present, defined by k preferably ranges from 2 to 4. Examples of carbonaceous material products are those having an attached aromatic sulfide organic group of the formula -(C6H4)-Sk-(C6H4)-, where k is an integer from 1 to 8, and more preferably where k ranges from 2 to 4. Other examples of aromatic sulfide groups are bis-para-(C6H4)-S2-(C6H4)- and para-(C6H4)-S2-(C6H5). The diazonium salts of these aromatic sulfidc groups may be conveniently prepared from their corresponding primary amines, H2N-Ar-S~-Ar'-NH2 or H2N-Ar-S~-Ar". Groups include dithiodi-4, l -phenylene, tetrathiodi-4,1-phenylene, phenyldithiophenylene, dithiodi-4,1-(3-chlorophenylene), -(4-C6H4)-S-S-(2-C7H4NS), -(4-CfiH4)-S-S-(4-C6H4)-OH, -6-(2-C7H3NS)-SH, -(4-C6H4)-CH2CH2-S-S-CH2CH2-(4-C6H4)-, -(4-C6H4)-CH2CH2-S-S-S-CH2CI-I 2-(4-C6H4)-, -(2-C6H4)-S-S-(2-C6H4)-, -(3-C6H4)-S-S-(3-C6H4)-, -6-(C6H3N2S), -6-(2-C7H3NS)-S-NRR' where RR' is -CH2CH20CH2CH2-, -(4-C6H4)-S-S-S-S-(4-C6H4)-, -(4-C6H4)-CH=CH 2~ -(4-C6H4)-S-S03H, -(4-C6H4)-S02NH-(4-C6H4)-S-S-(4-C6H4)-NHSO2-(4-C6H4)-,-6-(2-C7~I3NS)-S-S-2-(6-C7H3NS)-,-(4-C6H4)-S-CH2-(4-C6H4)-, -(4-C6H4)-SO2-S-(4-C6 H4)-, -(4-C6H4)-CH2-S-CH2-(4-C6H4)-, -(3-C6H4)-CH2-S-CH2 -(3-C6H4)- -(4-C6H4)-CH2-S-S-CH2-(4-C6H4)-, -(3-c6H4)-cH2-s-s-cH2-(3-c6H4)-~ -(4-C6H4) S
NRR', where RR' is -CH2CH20CH2CH2-, -(4-C6H4)-SO2NH-CH2CH2-S-S-CH2CH2-NHSO2-(4-C6H4)-, -(4-C6H4)-2-( 1,3 -dithianyl), and -(4-C6H4)-S-( 1 ,4-piperizinediyl)-S-(4-C6H4)-.
Another set of organic groups which may be attached to the carbonaceous material are organic groups having an aminophenyl, such as (C6H4)-NH2, (C6H4)-CH2-(C6H4)-NH2, (C6H4)-SO2-(C6H4)-NH2 Any one or more of these organic groups, after attachment to the carbonaceous material which permits adsorption, and preferably an increase in the adsorption capacity of the carbonaceous material may be used in the present invention.
SUBSTITUTE SH~ET (RULE 26) CA 022~8l89 l998-l2-l4 W 097/47382 -15- PCTrUS97/088S9 Preferably, the organic group attached to the carbonaceous material is an acid or base or a salt of an acid or base, and specific examples include phenyl or naphthyl groups having substituents like sulfonic acid, and carboxylic acid. Ql-~t~ rn~ry ammonium can also be used.
Most preferred organic groups ~ d to the carbonaceous material are (C6H4)-SO3~Na+, S (C6H4)-SO3-K+, (C6H4)-SO3-Li+, and the like. Generally, an acid-type organic group attachment will be useful in adsorbing basic adsorbates while a base-type organic group attachment will be useful in adsorbing acidic adsorbates.
A combination of different organic groups is possible. For instance, it is within the bounds of the present invention to attach more than one type of organic group to the satne 10 carbonaceous material or use a combination of carbonaceous materials, wherein some of the carbonaceous material has been modified with one organic group and another portion of the carbonaceous material has been modified with a different organic group. Varying degrees of modification are also possible, such as low weight percent or surface area modification, or a high weight percent or surface area modification. Also, mixtures of modified carbonaceous 15 material and unmodified carbonaceous material can be used.
Preferably, the modified carbonaceous materials of the present invention, especially when the attached organic group is a phenyl or naphthyl group having substituents like sulfonic acid, carboxylic acid, or quaternary ammonium or salts thereof, can be directly analogous to polymeric ion exchange resins. These types of carbonaceous materials of the 20 present invention can have one or more of the following properties as compared to conventional polymeric ion exchangers:
a) higher temperature stability;
b) greater resistance to swelling; and c) greater mechanical strength without adversely affecting uptake kinetics.

SUBSTITUTE SHEET (RULE 26) CA 022~8189 1998-12-14 W O 97147382 -16- PCTrUS97/088S9 Furthermore, the modified carbonaceous materials of the present invention, besides being used as adsorbents, can also be used in separations ranging from water treatment to metals separation/recovery, ion exchange, catalysis, and the like. An additional advantage of an adsorbent posse~ing exchangeable groups as described above is that it confers on the material the ability to be further surface modified using ion exchange procedures.
With respect to the adsorbates, any adsorbate capable of being adsorbed by one or more of the modified carbonaceous materials of the present invention is contemplated to be within the bounds of the present invention. Examples include, but are not limited to, polar species such as water, ammonia, melca~ s, sulfur dioxide, and hydrogen sulfide. By "polar species,"
it is understood that this is a species whose electronic structure is not symmetrical. This includes molecules that possess dipole moments, for example H2O and NH3; and/or molecules that possess quadrupole moments, such as CO2 and molecules that possess unsaturated pi bonds (B), such as alkenes, alkynes, and other organic and inorganic compounds with double and triple bonds. Non-polar species such as argon, oxygen, methane, and the like can also be adsorbed with the appropriate modified carbonaceous materials of the present invention. In view of the description provided in this application, those skilled in the art will be able to determine which organic groups need to be attached to the carbonaceous materials in order to achieve the most effective adsorption affinity or increase in adsorption, depending upon the adsorbate and the adsorption processes involved.
By developing an adsorbent composition containing a modified carbonaceous material capable of adsorbing an adsorbate, selectivity for a particular adsorbate can be enhanced.
Using the proper modified carbonaceous material, one can selectively adsorb particular species from a multicomponent mixture. In other words, modifying the carbonaceous material to create the adsorbent composition of the present invention can decrease adsorption affinity for one component in order to maximize the adsorption affinity of another component which will SUBSTITUTE Sl IEET (RULE 26) CA 022~8189 1998-12-14 W O 97/47382 PCTrUS97/08859 -17-m~ximi7~ separation of the second component from the first component. Furthermore, by increasing adsorption of polar species, this further results in the relatively decreased adsorption of nonpolar species which improves selectivity. Further, the carbonaceous material can be modified in such a manner as to add a hydrophobic group to "disable" the oxygen 5 functionalities on the surface of the carbonaceous material to increase the selectivity for the adsorption of nonpolar species.
The adsorbate can be in a liquid phase or in the gaseous or vapor phase, depending upon the needs and desires of the user. Certain adsorbates can be more efficiently adsorbed from the vapor or gaseous phases than from the liquid phase or vice versa, and the modified 10 carbonaceous materials of the present invention are effective in adsorption from either phase.
One advantage of the present invention is to modify the surface of an activated carbon or carbon black adsorbent extensively, without dzlm~ging the structure or making the adsorbent more friable. For instance, a carbonaceous material can be surface modified based on the present invention with exchangeable sodium cations attached to the surface. This is very 15 useful from the point of view of substituting different ions to alter the chemistry of the surface.
The beneficial effect of using the modified carbonaceous materials of the present invention for the purpose of adsorption can be demonstrated by comparing the adsorption isotherms of an adsorbate on an unmodified carbonaceous adsorbent and the same 20 carbonaceous adsorbent modified in accordance with the present invention.
The present invention will be further clarified by the following examples, which are int~n~ 1 to be purely exemplary of the present invention.
EXAMPLES
The effectiveness of the surface modification of exemplary carbonaceous material was ~5 determined by comparing the adsorption isotherms of various adsorbates on the unmodified SUBSTITUTE SHE~T (RULE 26) CA 022~8189 1998-12-14 W 097/47382 -18- PCTrUS97/088~9 carbonaceous materials, with adsorption isotherms on the carbonaceous materials modified in accordance with the present invention. Adsorbates used were water and CO2, but other adsorbates could also be used.
Example 1 Pellets of Black Pearls7 430 carbon black and Darco S51 activated carbon from Norit were surface-modified using the following procedure:
Surface modification of Black Pearls7 430 Carbon Black:
A dispersion of 5 ml of water dilutable phenol-formaldehyde thermosetting resin (Schenectady International, Schenectady, NY) in 50 mL of water was mixed with 50 g of Black Pearls7 430 carbon black (available *om Cabot Corp., Boston, MA). The mixture was pressed in 1 g portions using a 0.25 inch stainless steel die at a pressure of 5000 psi. The pellets were heated under flowing argon at 110~C for one hour and at 135~C for one hour to cure the resin. The temperature was then raised under flowing argon at 20~C/min until a temperature of 650~C was reached. The temperature was then held at 650~C for three hours and cooled under flowing argon. The pellets were then crushed into pieces about 1 mm by 2 mm.
An aqueous solution of 0.81 g of sodium nitrite in about 1 g of water was added to a mixture of 16.8 g of the carbon black granules, 2.04 g of sulfanilic acid, and 50 g of water that was stirring at 84~C. After stirring for two hours, the resulting material was dried in an oven at 65~C.
' Surface modification of activated carbon An aqueous solution of 30.5 g of sodium nitrite in about 100 g of water was added to a boiling mixture of 130 g of DARCO S51 activated carbon (available from Norit), 76.5 g of sulfanilic acid, and 1300 g of water. After stirring for 15 minutes, the heating was SUBSTITUTE SHEET (RULE 26) CA 022~8189 1998-12-14 W 097/47382 PCTrUS97/08859 discontinued and the mixture was allowed to cool to room temperature with stirring. The resulting material was dried overnight in an oven at 50~C.
Ion Exchan,ee:
The surface modified carbons were washed with a large amount of deionized water and 5 dried. The material thus obtained was in the sodium form. Further modification of the carbon into potassium and lithium forms was carried out by ion exchange using 2M solutions of KOH
and LiOH, respectively. The ion-exchanged material was washed thoroughly and dried.
Adsorption experiments were carried out on the washed, dried materials.
The surface areas of the unmodified and surface modified carbon materials are shown 10 in Table I below. Surface areas were calculated from nitrogen (77 K) adsorption data using the BET formalism (S.J. Gregg and K.S.W. Sing, in Adsorption~ Surface Area~ and Porosity,"
Academic Press, 1982). The adsorption experiments were carried out on an ASAP 2000 automated instrument, manufactured by Micromeritics Corp.

Table 1: Surface Areas and Pore Volumes of Unmodi~led and Surface Modi~led Materials BET Surface Pore Volume, Sample ~D Area, m2/g cm3/g BP 430 pellets, unmodified 99 0.518 BP 430, modified, washed 92 0.49 Darco S51 694 0.809 Darco S51, modified, washed 141.3 0.279 While the activated carbon lost some surface area and pore volume after the surface modification keatment, both the carbon black and the activated carbon underwent an increase in adsorption capacity per unit surface area as a result of the surface modification. The loss of any surface area and pore volume may be miti~tl~cl by pre-treating the carbonaceous SUBSTITUTE SI~ET (RULE 26) CA 022~8189 1998-12-14 W 097/47382 PCTnUS97/08859 material with immiscible organic solvent, like heptane. The results from adsorption of water vapor at 298 K on the unmodified and modified material are shown in Figure 1 (carbon black) and Figure 2 (activated carbon). The water adsorption experiments were carried out by a batch technique that involved equilibrating the sample with water vapor at a constant relative 5 humidity, in a sealed cell. The constant relative humidities were attained by using saturated salt solutions, which have known relative humidities above their surface.
Both the activated carbon and carbon black contained Na+ ions on the surface after the surface modification was carried out. The Na+ ions can be substituted by other ions using standard ion exchange procedures (e.g., see lon Exchan~e, by F. Helfferich, McGraw-Hill, 10 1962). The water adsorption isotherms for the surface-modifled material with Na+ ions on the surface, as well as the other ionic forms derived by ion exchange, are shown in Figures I
and 2. The adsorption isotherms show the quantity of water vapor adsorbed, per gram of adsorbent, as a function of the relative pressure of water vapor. Figures 3 and 4 show the sarne data normalized by the BET surface area of the materials. It is clear that the adsorption 15 capacities per unit area of the carbon black, Black Pearls7 430 carbon black and the Darco S51 carbon black, are considerably enhanced by the surface modification described in this invention. In addition, the shape of the water adsorption isotherm is changed as a result of the surface modification (concave upward, to linear or convex upward).
The surface modification technique of the present invention may affect the adsorption 20 of gases like CO2 as well, which possesses a quadrupole movement. Figure 5 shows the adsorption isotherm of CO2 from the gas phase at 273 K on the same unmodified and modified Black Pearls7 430 carbon black. Adsorption of CO2 was carried out on an ASAP 2000 automated adsorption system manufactured by Micromeritics Corp. The figure shows the quantity of CO2 adsorbed as a function of the CO2 pressure. Clearly, the adsorption of CO2 25 is enhanced by the carbon surface modification technique described in this invention.
SUBSTITUTE SHEET (RULE 26) Other embodiments of the present invention will be a~palelll to those skilled in the art from consideration of the specification and practice of the invention disclosed herein. It is intt?n~1~d that the specification and examples be considered as exemplary only, with a true scope and spirit of the invention being indicated by the following claims.

SUBSTITUTE SHEET tRULE 26)

Claims (27)

WHAT IS CLAIMED IS:
1. An adsorbent composition comprising a modified carbonaceous material capable of adsorbing an adsorbate wherein at least one organic group is attached to said modified carbonaceous material.
2. The adsorbent composition of claim 1, wherein said organic group is (C6H4)-SO3-Na+, (C6H4)-SO3-Li+, or (C6H4)SO3-K+.
3. The adsorbent composition of claim 1, wherein said organic group is p-C6H4SO2NH2 or -C6H4NH2.
4. The adsorbent composition of claim 1, wherein said organic group is hydrophilic.
5. The adsorbent composition of claim 1, wherein said modified carbonaceous material is activated carbon or carbon black.
6. A method to increase the adsorption capacity of a carbonaceous material capable of adsorbing an adsorbate comprising attaching to said carbonaceous material at least one organic group capable of increasing said adsorption capacity.
7. The method of claim 6, wherein said carbonaceous material is activated carbon or carbon black.
8. The method of claim 6, wherein said organic group is (C6H4)-SO3-Na', (C6H4)-SO3-Li+, or (C6H4)SO3-K+.
9. The method of claim 6, wherein said organic group is p-C6H4SO2NH2 or -C6H4NH2.
10. The method of claim 6, wherein said organic group is hydrophilic.
11. The method of claim 6, wherein said adsorbate is polar.
12. The method of claim 6, wherein said adsorbate is water, ammonia, carbon dioxide, sulfur dioxide, or hydrogen sulfide.
13. The method of claim 12, wherein said adsorbate is water.
14. The method of claim 6, wherein said adsorbate is non-polar.
15. The method of claim 14, wherein said adsorbate is argon, oxygen, or methane.
16. The method of claim 6, wherein said adsorbate is in the gas or vapor phase.
17. The method of claim 6, wherein said adsorbate is in the liquid phase.
18. A method to adsorb an adsorbate comprising contacting said adsorbate with a modified carbonaceous material capable of adsorbing said adsorbate wherein at least one organic group is attached to said modified carbonaceous material.
19. The method of claim 18, wherein said modified carbonaceous material is activated carbon or carbon black.
20. The method of claim 18, wherein said organic group is (C6H4)-SO3-Na+, (C6H4)-SO3-Li+, or (C6H4)SO3-K+.
21. The method of claim 18, wherein said organic group is p-C6H4SO2NH2 or -C6H4NH2.
22. The method of claim 18, wherein said organic group is hydrophilic.
23. The method of claim 18, wherein said adsorbate is polar.
24. The method of claim 18, wherein said adsorbate is water, ammonia, carbon dioxide, hydrogen sulfide, argon, oxygen, or methane.
25. The method of claim 24, wherein said adsorbate is water.
26. The adsorbent composition of claim 1, wherein said organic group contains an exchangeable ion.
27. An ion exchange material comprising the adsorbent composition of claim 26.
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Families Citing this family (52)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6008272A (en) * 1995-05-22 1999-12-28 Cabot Corporation Elastomeric compounds incorporating silicon-treated carbon blacks
US5955232A (en) * 1997-07-22 1999-09-21 Cabot Corporation Toners containing positively chargeable modified pigments
US6218067B1 (en) 1998-11-06 2001-04-17 Cabot Corporation Toners containing chargeable modified pigments
EP2316875A1 (en) 1999-01-20 2011-05-04 Cabot Corporation Aggregates having attached polymer groups and polymer foams
JP2002535430A (en) 1999-01-20 2002-10-22 キャボット コーポレイション Aggregates with attached polymer groups and polymer foam
EP1250189B1 (en) * 2000-01-17 2005-06-22 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Method for modifying the surfaces of fine-porous adsorbents
JP2001224958A (en) * 2000-02-14 2001-08-21 Isuzu Ceramics Res Inst Co Ltd Co2 adsorbent
JP4747402B2 (en) * 2000-08-08 2011-08-17 株式会社ブリヂストン Adsorbent for aldehydes
AU2001288672A1 (en) * 2000-09-01 2002-03-13 Cabot Corporation Chromatography and other adsorptions using modified carbon adsorbents
CA2420916A1 (en) * 2000-09-01 2002-03-07 Cabot Corporation Chromatography and other adsorptions using modified carbon-clad metal oxide particles
DE10133773A1 (en) * 2001-07-16 2003-02-20 Freudenberg Carl Kg Regularly structured nonwovens, processes for their production and their use
US6787029B2 (en) 2001-08-31 2004-09-07 Cabot Corporation Material for chromatography
WO2005018802A2 (en) * 2003-08-25 2005-03-03 Cabot Corporation Compositions and chromatography materials for bioseparation
US7300504B2 (en) * 2003-10-20 2007-11-27 Cabot Corporation Inkjet inks and methods of preparing the same
US20060289003A1 (en) * 2004-08-20 2006-12-28 Lackner Klaus S Laminar scrubber apparatus for capturing carbon dioxide from air and methods of use
US20060051274A1 (en) * 2004-08-23 2006-03-09 Wright Allen B Removal of carbon dioxide from air
US7655069B2 (en) * 2005-02-02 2010-02-02 Global Research Technologies, Llc Removal of carbon dioxide from air
WO2007018558A2 (en) * 2005-07-20 2007-02-15 The Trustees Of Columbia University In The City Of New York Electrochemical recovery of carbon dioxide from alkaline solvents
ES2638792T3 (en) * 2005-07-28 2017-10-24 Carbon Sink Inc. Removal of carbon dioxide from the air
US9266051B2 (en) 2005-07-28 2016-02-23 Carbon Sink, Inc. Removal of carbon dioxide from air
EP2668992A3 (en) 2006-03-08 2014-04-02 Kilimanjaro Energy, Inc. Air collector with functionalized ion exchange membrane for capturing ambient CO2
CN104826450B (en) * 2006-10-02 2021-08-27 碳汇公司 Extraction of CO from air2Method and apparatus
EP2097157A4 (en) * 2006-11-15 2011-02-02 Global Res Technologies Llc Removal of carbon dioxide from air
US20080115872A1 (en) * 2006-11-16 2008-05-22 Paul Harry Sandstrom Butyl rubber which contains organoperoxide and isobutyene adsorbing activated carbon, pneumatic tire with built-in sealant and method
US7531596B2 (en) * 2006-11-30 2009-05-12 The Goodyear Tire & Rubber Company Rubber composition containing antidegradant and MIBK adsorbing activated carbon, and pneumatic tire with component
US7595360B2 (en) * 2006-11-30 2009-09-29 The Goodyear Tire & Rubber Company Rubber composition containing diene-based elastomer, precipitated silica, coupling agent and alcohol-adsorbing activated carbon and pneumatic tire with component
US20080128065A1 (en) * 2006-11-30 2008-06-05 Paul Harry Sandstrom Pneumatic tire with oxygen barrier component comprised of a rubber composition containing a dispersion of oxygen-adsorbing activated carbon
US8080088B1 (en) * 2007-03-05 2011-12-20 Srivats Srinivasachar Flue gas mercury control
AU2008242845B2 (en) 2007-04-17 2012-08-23 Carbon Sink, Inc. Capture of carbon dioxide (CO2) from air
EP2212009A1 (en) * 2007-11-05 2010-08-04 Global Research Technologies, LLC Removal of carbon dioxide from air
JP2011504140A (en) * 2007-11-20 2011-02-03 グローバル リサーチ テクノロジーズ,エルエルシー Air collector with functional ion exchange membrane to capture ambient CO2
WO2009105566A2 (en) 2008-02-19 2009-08-27 Global Research Technologies, Llc Extraction and sequestration of carbon dioxide
WO2009149292A1 (en) * 2008-06-04 2009-12-10 Global Research Technologies, Llc Laminar flow air collector with solid sorbent materials for capturing ambient co2
US20110203174A1 (en) * 2008-08-11 2011-08-25 Lackner Klaus S Method and apparatus for extracting carbon dioxide from air
US20110206588A1 (en) * 2008-08-11 2011-08-25 Lackner Klaus S Method and apparatus for removing ammonia from a gas stream
US20110203311A1 (en) * 2008-08-22 2011-08-25 Wright Allen B Removal of carbon dioxide from air
US8916493B2 (en) * 2008-09-08 2014-12-23 Amminex Emissions Technology A/S Additives for highly compacted ammonia storage materials
WO2012006417A2 (en) 2010-07-07 2012-01-12 The Regents Of The University Of Colorado, A Body Corporate Metal removal system and method
KR101780185B1 (en) * 2010-12-10 2017-09-21 삼성전자주식회사 Absorbent shell and manufacturing method thereof
US8679231B2 (en) 2011-01-19 2014-03-25 Advanced Technology Materials, Inc. PVDF pyrolyzate adsorbent and gas storage and dispensing system utilizing same
CA2859042A1 (en) * 2011-12-23 2013-06-27 Tusaar Inc. System for dynamic fluidized loading of a ligand upon carbon media and methods associated therewith
WO2013181295A1 (en) * 2012-05-29 2013-12-05 Advanced Technology Materials, Inc. Carbon adsorbent for hydrogen sulfide removal from gases containing same, and regeneration of adsorbent
US9073039B2 (en) * 2012-07-13 2015-07-07 Adavanced Fuel Research, Inc. Carbon sorbent for reversible ammonia sorption
US9186650B2 (en) 2013-04-05 2015-11-17 Entegris, Inc. Adsorbent having utility for CO2 capture from gas mixtures
CN103769065A (en) * 2014-01-21 2014-05-07 同济大学 Active carbon modification method for improving adsorption rate of non-polar molecules
US9289714B1 (en) 2014-10-17 2016-03-22 JuvanCo Industries, LLC Device for adsorbing the hydrogen sulfide component of exhausted calibration gases
WO2019161114A1 (en) 2018-02-16 2019-08-22 Carbon Sink, Inc. Fluidized bed extractors for capture of co2 from ambient air
KR102207340B1 (en) * 2018-10-19 2021-01-22 한남대학교 산학협력단 a surface-modified porous carbon composite materials and a method manufacturing the same
WO2020154493A1 (en) * 2019-01-25 2020-07-30 Tusaar Corp. Highly-functionalized carbon materials for the removal of inorganic and organic contaminants
US10822807B2 (en) 2019-02-18 2020-11-03 Royal Building Products (Usa) Inc. Assembly for improved insulation
KR102183149B1 (en) * 2019-04-17 2020-11-25 한남대학교 산학협력단 a porous carbon composite materials for canister and a method manufacturing the same
KR102540341B1 (en) * 2021-02-28 2023-06-05 한남대학교 산학협력단 a water purification device comprising metal complex filter using 3D printing

Family Cites Families (159)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1999573A (en) 1930-08-29 1935-04-30 William W Odell Special carbon black
US2121535A (en) 1934-09-22 1938-06-21 Cabot Godfrey L Inc Granular product and method of preparing the same
US2156591A (en) 1936-06-29 1939-05-02 Sealco By Products Company Manufacture of carburized silica
US2375795A (en) 1941-12-22 1945-05-15 Phillips Petroleum Co Carbon black process
US2502254A (en) 1945-12-07 1950-03-28 Ici Ltd Manufacture of pigments
US2564700A (en) 1947-04-25 1951-08-21 Phillips Petroleum Co Production of carbon black
US2514236A (en) 1948-03-12 1950-07-04 Ici Ltd Manufacture of pigments
US2632713A (en) 1948-10-29 1953-03-24 Phillips Petroleum Co Carbon black process
DE957755C (en) 1949-06-08 1957-01-17 W. R. Grace a Co., New York, N. Y. (V. St. A.) Process for the production of a silica gel suitable as a matting agent for paints or the like
US2793100A (en) 1952-10-16 1957-05-21 Degussa Process of modifying carbon black
US2833736A (en) 1953-07-20 1958-05-06 Western Union Telegraph Co Aqueous graphite-polyvinyl alcohol ink composition
US3011902A (en) 1954-05-27 1961-12-05 Cabot Corp Process of manufacturing carbon black pellets for inks
US2867540A (en) 1955-12-30 1959-01-06 Monsanto Chemicals Modified carbon black product and process
US2891595A (en) 1956-07-31 1959-06-23 Exxon Research Engineering Co Chlorinated rubbery copolymers
US3094428A (en) 1957-06-07 1963-06-18 Monsanto Chemicals Composition of metal oxides and carbon black
US3043708A (en) 1958-07-22 1962-07-10 Dunlop Rubber Co Modified carbon black
GB910309A (en) 1958-07-22 1962-11-14 Dunlop Rubber Co Rubber compositions
BE626217A (en) 1961-12-18 1900-01-01
US3317458A (en) 1963-10-07 1967-05-02 Degussa Mixture of carbon black and light filler aqueous suspension added to rubber latex
US3335020A (en) 1964-03-02 1967-08-08 Huber Corp J M Modified carbon blacks
US3674670A (en) 1964-12-04 1972-07-04 Ppg Industries Inc Coating method
US3390006A (en) 1965-08-30 1968-06-25 Huber Corp J M Method of making carbon black/silica pigment
US3479300A (en) 1965-10-22 1969-11-18 Cabot Corp Carbonaceous products
UST860001I4 (en) 1966-12-22 1969-03-18 Defensive publication
US3528840A (en) 1967-11-15 1970-09-15 Huber Corp J M Sulfonated carbon black
DE1792148A1 (en) 1968-07-27 1971-10-21 Degussa Improved pre-wetted pigment preparations
US3622650A (en) 1969-02-04 1971-11-23 Cabot Corp Rubber reinforcing compositions
US3607813A (en) 1969-09-05 1971-09-21 Union Carbide Corp Printing ink compositions
DE1948443C3 (en) 1969-09-25 1981-02-19 Degussa Ag, 6000 Frankfurt Process for the production of highly dispersed, homogeneous mixtures consisting of or containing silicon dioxide and carbon black
US3876603A (en) 1970-06-22 1975-04-08 Ppg Industries Inc Method of encapsulating pigments in organic dispersions of polymers
US3686111A (en) 1970-06-22 1972-08-22 Ppg Industries Inc Non-aqueous polymeric pseudo-dispersion
US4014844A (en) 1970-06-26 1977-03-29 Agence Nationale De Valorisation De La Recherche (Anvar) Process for grafting polymers on carbon black through free radical mechanism
US3716513A (en) 1970-07-16 1973-02-13 O Burke Silica pigments and elastomer-silica pigment masterbatches and production processes relating thereto
US3689452A (en) 1970-07-16 1972-09-05 Burke Oliver W Jun Elastomer-silica pigment masterbatches and production processes relating thereto
US3846141A (en) 1970-12-07 1974-11-05 Dick Co Ab Jet printing ink composition
US3997356A (en) 1971-08-17 1976-12-14 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler Reinforcing additive
US3873489A (en) 1971-08-17 1975-03-25 Degussa Rubber compositions containing silica and an organosilane
JPS5322553B2 (en) * 1973-04-20 1978-07-10
GB1506464A (en) 1974-05-29 1978-04-05 Degussa Aqueous carbon black preparation
US4003751A (en) 1974-09-05 1977-01-18 Union Carbide Corporation Coating and ink compositions
US4074035A (en) 1975-04-22 1978-02-14 Exxon Research & Engineering Co. Halomethylated aromatic interpolymers
JPS51137506A (en) 1975-05-22 1976-11-27 Konishiroku Photo Ind Composition of ink for ink jet recording
DE2536674C3 (en) 1975-08-18 1979-09-27 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler, 6000 Frankfurt Crosslinkable mixtures based on rubber, organosilanes and silicate fillers
US4014833A (en) 1975-11-28 1977-03-29 Owens-Illinois, Inc. Aqueous printing ink with polyethylene oxide
US4061830A (en) 1975-12-23 1977-12-06 Ppg Industries, Inc. Selective solar energy receiver and method for its production
US4071496A (en) 1976-04-30 1978-01-31 Phillips Petroleum Company Carbon black for low-hysteresis rubber compositions
US4108679A (en) 1976-11-22 1978-08-22 Ebonex Corporation Pigment composition containing elemental carbon and process of making the same
US4204871A (en) 1978-04-04 1980-05-27 Sun Chemical Corporation Printing inks containing nucleated organic pigments
US4204876A (en) 1978-07-17 1980-05-27 M. Hamburger & Sons, Inc. Cement coloring composition and method of producing same
US4211578A (en) 1979-06-08 1980-07-08 J. M. Huber Corporation Method of producing a carbon black silica pigment
JPS5626972A (en) * 1979-08-13 1981-03-16 Mitsubishi Rayon Co Ltd Oil-containing waste water-treating material comprising modified active carbon
DE2933346C2 (en) 1979-08-17 1982-07-01 Degussa Ag, 6000 Frankfurt Silane / filler preparations, processes for their production and application of the same
JPS5682859A (en) 1979-12-11 1981-07-06 Sakura Color Prod Corp Ink composition
US4265768A (en) * 1979-12-26 1981-05-05 Rohm And Haas Company Ion exchange material prepared from partially pyrolyzed macroporous polymer particles
US4290072A (en) 1980-01-28 1981-09-15 American Can Company Opaque jet ink printing method and composition
JPS592451B2 (en) 1980-01-30 1984-01-18 株式会社ブリヂストン rubber composition
US4293394A (en) 1980-03-31 1981-10-06 Ppg Industries, Inc. Electrolytically producing chlorine using a solid polymer electrolyte-cathode unit
DE3115532A1 (en) 1980-04-17 1982-01-28 Canon K.K., Tokyo INK-JET RECORDING METHOD AND RECORDING INK FOR RECORDING ON AN IMAGE RECEIVER
US4478905A (en) 1980-04-21 1984-10-23 Ppg Industries, Inc. Spandrel product with silicate coating
US4476270A (en) 1980-06-06 1984-10-09 E. I. Du Pont De Nemours And Company Process for making high solids acrylic dispersion lacquer
US4328041A (en) 1980-06-09 1982-05-04 Milliken Research Corporation Comminuted inorganic materials
JPS5938016B2 (en) * 1980-11-10 1984-09-13 呉羽化学工業株式会社 Collecting agent and method for collecting and concentrating basic malodorous components
JPS5821434A (en) 1981-07-31 1983-02-08 Japan Synthetic Rubber Co Ltd Polybutadiene rubber composition
EP0098338B1 (en) 1982-07-09 1988-04-20 Battelle Memorial Institute Low viscosity stable aqueous dispersion of graft carbon black
DE3228723A1 (en) 1982-07-31 1984-02-02 Basf Farben + Fasern Ag, 2000 Hamburg STORAGE-STABLE, HEAT-CURABLE MATERIAL MIXTURES MADE OF POLYISOCYANATE AND COMPOUNDS WITH REACTIVE COMPOSITIONS, METHOD FOR THE PRODUCTION AND USE THEREOF
WO1984000770A1 (en) 1982-08-09 1984-03-01 Ford Werke Ag High solids coating compositions
US4710543A (en) 1982-08-09 1987-12-01 E. I. Du Pont De Nemours And Company Glycidyl-hydroxy-acrylic high solids coating compositions
US4451597A (en) 1982-11-15 1984-05-29 E. I. Du Pont De Nemours And Company High solids color coat containing alcohol soluble cellulose acetate butyrate
US4442256A (en) 1982-12-16 1984-04-10 E. I. Du Pont De Nemours And Company Additive for alkyd resin coating compositions
US4605596A (en) 1982-12-20 1986-08-12 E. I. Du Pont De Nemours And Company Additive for coating compositions
US4528281A (en) * 1983-03-16 1985-07-09 Calgon Carbon Corporation Carbon molecular sieves and a process for their preparation and use
DE3311513A1 (en) 1983-03-30 1984-10-04 Basf Farben + Fasern Ag, 2000 Hamburg HEAT-CURABLE COATING AGENTS AND THEIR USE
DE3319251C1 (en) 1983-05-27 1984-04-19 Degussa Ag, 6000 Frankfurt Vulcanizable halogen rubber compounds and methods for vulcanizing or crosslinking
US4503174A (en) 1983-09-06 1985-03-05 E. I. Du Pont De Nemours And Company Low temperature curing coating composition
US4680204A (en) 1983-09-06 1987-07-14 Ppg Industries, Inc. Color plus clear coating system utilizing inorganic microparticles
US4525521A (en) 1983-10-14 1985-06-25 E. I. Du Pont De Nemours And Company Coating composition of an acrylic polymer having amino ester groups and a glycidyl acrylic polymer
US4556427A (en) 1983-12-12 1985-12-03 Union Camp Corporation Use of humates in printing inks
US4503175A (en) 1983-12-19 1985-03-05 E. I. Du Pont De Nemours And Company Acrylic polyurethane coating composition
US4555535A (en) 1984-03-07 1985-11-26 E. I. Du Pont De Nemours And Company Acrylic polyurethane coating composition
US4620994A (en) 1984-03-30 1986-11-04 Ppg Industries, Inc. Color plus clear coating system utilizing organo-modified clay
US4620993A (en) 1984-03-30 1986-11-04 Ppg Industries, Inc. Color plus clear coating system utilizing organo-modified clay in combination with organic polymer microparticles
FR2562534B1 (en) 1984-04-06 1986-06-27 Rhone Poulenc Chim Base NOVEL PRECIPITATED SILICA WITH IMPROVED MORPHOLOGICAL CHARACTERS, PROCESS FOR OBTAINING THE SAME AND APPLICATION THEREOF, IN PARTICULAR AS FILLER
JPS60260499A (en) 1984-06-07 1985-12-23 Idemitsu Kosan Co Ltd Preparation of sic whisker
US4665128A (en) 1984-09-17 1987-05-12 E. I. Du Pont De Nemours And Company Flexible coating compositions
US4719132A (en) 1984-09-21 1988-01-12 Ppg Industries, Inc. Process for the preparation of multi-layered coatings and coated articles derived therefrom
US4692481A (en) 1984-09-27 1987-09-08 E. I. Du Pont De Nemours And Company Process for matching color of paint to a colored surface
US4741780A (en) 1985-02-11 1988-05-03 Atkinson George K Treatment of titanium dioxide and other pigments to improve dispersibility
US5026755A (en) * 1985-03-13 1991-06-25 Sun Chemical Corporation Water-based printing ink prepared from polyamide/acrylic graft copolymers
US5008335A (en) * 1985-08-07 1991-04-16 Ppg Industries, Inc. Powder coating compositions of polyepoxides, acrylic copolymers and aliphatic or polyester dibasic acids
US4681811A (en) 1985-08-19 1987-07-21 Ppg Industries, Inc. Color plus clear coatings employing polyepoxides and polyacid curing agents in the clear coat
US4650718A (en) 1985-08-19 1987-03-17 Ppg Industries, Inc. Color plus clear coatings employing polyepoxides and polyacid curing agents
DE3545618A1 (en) * 1985-12-21 1987-06-25 Basf Lacke & Farben WATER-DISCOVERABLE COATING AGENT FOR PRODUCING THE BASE LAYER OF A MULTILAYER COATING
US4659770A (en) 1986-02-03 1987-04-21 E.I. Du Pont De Nemours And Company Coating composition of an amine polymer and a blocked polyisocyanate
US4670059A (en) 1986-02-11 1987-06-02 Hewlett Packard Company Increased solubility of carbon black
JPS62191040A (en) * 1986-02-17 1987-08-21 Nippon Denso Co Ltd Adsorbable carbon material and its production
US4764430A (en) 1986-03-07 1988-08-16 Ppg Industries, Inc. Crosslinkable compositions containing polyepoxides and polyacid curing agents
US4702749A (en) 1986-06-24 1987-10-27 Air Products And Chemicals, Inc. Technique for surface oxidation of activated carbon
US4727100A (en) 1986-08-15 1988-02-23 E. I. Du Pont De Nemours And Company Coating composition containing a reactive urethane component an acrylic fatty acid drying oil resin and a metallic alkylate
DE3629470A1 (en) * 1986-08-29 1988-03-10 Basf Lacke & Farben CARBOXYL GROUPS AND TERTIAL AMINO GROUPS CONTAINING POLYCONDENSATION AND / OR ADDITION PRODUCT, COATING AGENTS BASED ON THE SAME AND THEIR USE
DE3636726C1 (en) 1986-10-29 1988-03-17 Pelikan Ag Aqueous writing fluids and a process for their preparation
US4752532A (en) 1986-10-31 1988-06-21 E. I. Du Pont De Nemours And Company Polyester primer composition
US4880857A (en) * 1986-12-17 1989-11-14 Nippon Shokubai Kagaku Kogyo Co., Ltd. Carbon black-graft polymer, method for production thereof, and use thereof
JPS63156841A (en) * 1986-12-22 1988-06-29 Yokohama Rubber Co Ltd:The Pneumatic radial tire
JPH0832804B2 (en) 1987-02-24 1996-03-29 横浜ゴム株式会社 Rubber composition
JPH068366B2 (en) 1987-04-23 1994-02-02 株式会社ブリヂストン Rubber composition for tires
US4808656A (en) 1987-05-04 1989-02-28 Ppg Industries, Inc. High solids coating compositions
US4840674A (en) * 1987-06-01 1989-06-20 Xerox Corporation Ink compositions
US4789400A (en) 1987-07-10 1988-12-06 Xerox Corporation Waterfast ink jet compositions and process
US4927868A (en) * 1987-08-19 1990-05-22 Ppg Industries, Inc. High solids coating compositions containing a polyepoxide and a copolymer of an alpha-olefin and an olefinically unsaturated monoanhydride
US4798746A (en) 1987-08-24 1989-01-17 Ppg Industries, Inc. Basecoat/clearcoat method of coating utilizing an anhydride additive in the thermoplastic polymer-containing basecoat for improved repairability
US4798745A (en) 1987-08-24 1989-01-17 Ppg Industries, Inc. Non-yellowing coating composition based on a hydroxy component and an anhydride component and utilization in a process of coating
US5093391A (en) * 1988-06-27 1992-03-03 E. I. Du Pont De Nemours And Company Multi-component coating composition comprising an anhydride containing polymer, a glycidyl component and an acid functional component
US5017435A (en) * 1988-06-27 1991-05-21 E. I. Du Pont De Nemours And Company Multi-component coating composition comprising an anhydride containing polymer, a glycidyl component and a monomeric or oligomeric anhydride component
US4908397A (en) * 1988-06-27 1990-03-13 E. I. Du Pont De Nemours And Company Multi-component coating composition comprising an anhydride containing polymer, a glycidyl component and a self-stabilized dispersion resin
US4894420A (en) * 1988-09-14 1990-01-16 The Goodyear Tire & Rubber Company Tire with tread of selective rubber blend
DE3906818C2 (en) * 1989-03-03 1994-01-13 Degussa Gray-black inclusion pigments and process for their preparation
US5204404A (en) * 1989-03-21 1993-04-20 E. I. Du Pont De Nemours And Company Waterbased acrylic silane and polyurethane containing coating composition
DE69006788T2 (en) * 1989-07-24 1994-07-07 Sumitomo Chemical Co Rubber compound with excellent dynamic properties.
DE3924618A1 (en) * 1989-07-26 1991-01-31 Basf Lacke & Farben COATING AGENTS BASED ON CARBOXYL GROUP-CONTAINING POLYMERS AND EPOXY GROUP GROUPING NETWORKS, METHOD FOR PRODUCING THE COATING AGENT AND ITS USE
JP2889326B2 (en) * 1989-09-14 1999-05-10 昭和キャボット株式会社 Carbon black and rubber composition
US5238888A (en) * 1989-10-02 1993-08-24 Kuraray Chemical Co., Ltd. Carbon molecular sieve
ES2049885T3 (en) * 1989-10-19 1994-05-01 Canon Kk INK AND METHOD FOR INK JET PRINTING, INK CARTRIDGE, INK JET DEVICE AND APPARATUS FOR INK JET PRINTING USING THEM.
DE59009466D1 (en) * 1989-10-26 1995-09-07 Ciba Geigy Ag Aqueous printing inks for inkjet printing.
WO1991007470A1 (en) * 1989-11-21 1991-05-30 Seiko Epson Corporation Ink for use in ink jet recording
CA2072567C (en) * 1990-01-08 2001-10-23 Chiung-Huei Shieh Carbon blacks imparting superior treadwear/hysteresis performance
US5200164A (en) * 1990-04-04 1993-04-06 Cabot Corporation Easily dispersible carbon blacks
US5182355A (en) * 1990-04-05 1993-01-26 Ppg Industries, Inc. Polyurethane polyanhydride oligomers and method of preparation
JP2565587B2 (en) * 1990-08-06 1996-12-18 竹内精工 株式会社 Linear motion ball bearing and manufacturing method thereof
US5281261A (en) * 1990-08-31 1994-01-25 Xerox Corporation Ink compositions containing modified pigment particles
US5100470A (en) * 1990-10-25 1992-03-31 Hewlett-Packard Company Waterfast ink formulations for thermal ink-jet using organic amines
US5314945A (en) * 1990-12-03 1994-05-24 E. I. Du Pont De Nemours And Company Waterbased coating compositions of methylol(meth)acrylamide acrylic polymer, polyurethane and melamine crosslinking agent
US5290848A (en) * 1990-12-18 1994-03-01 E. I. Du Pont De Nemours And Company Coating composition of a glycidyl acrylic polymer, an aminoester acrylic polymer and a polyester or a polyesterurethane
US5206295A (en) * 1991-02-25 1993-04-27 E. I. Du Pont De Nemours And Company Coating composition comprising an anhydride-containing polymer and a structured epoxy-containing polymer
US5135548A (en) * 1991-05-08 1992-08-04 Air Products And Chemicals, Inc. Oxygen selective desiccants
US5286286A (en) * 1991-05-16 1994-02-15 Xerox Corporation Colorless fast-drying ink compositions for printing concealed images detectable by fluorescence
DE4119959A1 (en) * 1991-06-18 1992-12-24 Degussa METHOD FOR PRODUCING VULCANIZABLE, RUSSELED PLASTIC AND RUBBER MIXTURES
US5114477A (en) * 1991-09-03 1992-05-19 Xerox Corporation Liquid ink compositions
US5314953A (en) * 1991-10-21 1994-05-24 E. I. Du Pont De Nemours And Company Clear coating composition for clear coat/color coat finish
DE4222372A1 (en) * 1992-07-08 1994-01-13 Merck Patent Gmbh Carbon black pigments
US5310778A (en) * 1992-08-25 1994-05-10 E. I. Du Pont De Nemours And Company Process for preparing ink jet inks having improved properties
US5294253A (en) * 1992-11-06 1994-03-15 Hydril Company Carbon black system and improved rubber stock
US5302197A (en) * 1992-12-30 1994-04-12 E. I. Du Pont De Nemours And Company Ink jet inks
US5401313A (en) * 1993-02-10 1995-03-28 Harcros Pigments, Inc. Surface modified particles and method of making the same
GB9313871D0 (en) * 1993-07-05 1993-08-18 Secr Defence Substituted activated carbons
AU1601595A (en) * 1994-01-10 1995-08-01 Hemasure, Inc. Device and process for removing leukocytes and viral inactivating agents from blood
US5447557A (en) * 1994-03-23 1995-09-05 Air Products And Chemicals, Inc. Oxygen selective adsorbents
IL116376A (en) * 1994-12-15 2001-03-19 Cabot Corp Aqueous ink jet ink compositions containing modified carbon products
US5559169A (en) * 1994-12-15 1996-09-24 Cabot Corporation EPDM, HNBR and Butyl rubber compositions containing carbon black products
IL116378A (en) * 1994-12-15 2003-05-29 Cabot Corp Non-aqueous coating or ink composition with improved optical properties containing modified carbon product and method of preparation of the composition
IL154538A (en) * 1994-12-15 2009-12-24 Cabot Corp Reaction of carbon black with diazonium salts, resultant carbon black products and their uses
US5571311A (en) * 1994-12-15 1996-11-05 Cabot Corporation Ink jet ink formulations containing carbon black products
US5575845A (en) * 1994-12-15 1996-11-19 Cabot Corporation Carbon black products for coloring mineral binders
US5554739A (en) * 1994-12-15 1996-09-10 Cabot Corporation Process for preparing carbon materials with diazonium salts and resultant carbon products
US5972826A (en) * 1995-03-28 1999-10-26 Cabot Corporation Densified carbon black adsorbent and a process for adsorbing a gas with such an adsorbent
AR002061A1 (en) * 1995-05-22 1998-01-07 Cabot Corp ELASTOMERIC COMPOUND INCORPORATING PARTIALLY COATED CARBON BLACK, AN ARTICLE FORMED FROM SUCH A COMPOUND, A FORMULATION CONTAINING IT AND A METHOD FOR IMPROVING HYSTERESIS.
US5622557A (en) * 1995-05-22 1997-04-22 Cabot Corporation Mineral binders colored with silicon-containing carbon black
US5877238A (en) * 1995-05-22 1999-03-02 Cabot Corporation Elastomeric compounds incorporating silicon-treated carbon blacks and coupling agents
JPH0915389A (en) * 1995-06-27 1997-01-17 Japan Atom Energy Res Inst Radioactive nuclide adsorbent and its production method and volume reduction processing method for radioactive waste
DE19610477A1 (en) * 1996-03-16 1997-09-18 Rico Mikroelektronik Gmbh Expandable shell for inside sewer pipe renovation

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