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Claims  |
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I claim:
1. A positively-charged water-soluble graft copolymer of lignin with an
anion, having a central lignin network and at least one grafted side chain
having randomly repeating units of the formulas:
##STR9##
wherein the ratio of such repeating units range from about one molar
percent to about 100 molar percent, and from about zero molar percent to
about 99 molar percent, respectively, such that the central lignin network
has a molecular weight of about 1,000 to 150,000 and the total number of
randomly repeating units in the grafted side chain or chains is in the
range of 50 to 300,000 units, and such that the total graft copolymer
molecular weight is in the range of 15,000 to 30,000,000.
2. A copolymer as called for in claim 1, wherein said lignin used as the
central network is selected from the group consisting of alkali lignin,
HCl lignin, milled-wood lignin and 1,4-dioxane lignin.
3. A copolymer as called for in claim 1, wherein said anion is selected
from a group consisting of chloride, methylsulfate, bromide, nitrate and
bicarbonate.
4. A method of preparing a positively-charged water-soluble graft copolymer
of lignin which comprises free radically graft copolymerizing
2-propenamide and 2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene
with a neutralizing anion on lignin.
5. A method as called for in claim 4, wherein said step of copolymerizing
comprises:
(a) adding a hydroperoxide to a solvent; and
(b) adding lignin, a chloride-containing salt, 2-propenamide and
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene chloride or
methylsulfate to said solvent, thereby initiating free radical
polymerization.
6. A method as called for in claim 5 wherein the components are added in
sufficient quantity such that the chloride ion concentration of the
reaction mixture ranges from about 1.37 weight percent to about 1.5 weight
percent.
7. A method as called for in claim 5 wherein the components are added in
sufficient quantity such that the chloride-containing salt content of the
reaction mixture ranges from about 0.47 weight percent to about 0.92
weight percent.
8. A method as called for in claim 5 further comprising adding an aqueous
solution of at least one selected from the group consisting of ceric,
vanadium and manganese ions.
9. A method as called for in claim 5 wherein said hydroperoxide is selected
from the group consisting of inorganic hydroperoxide and t-butyl
hydroperoxide.
10. A method as called for in claim 5 wherein said copolymerization is
allowed to proceed for about one hour to about 200 hours and is terminated
by the addition of a free radical scavenger.
11. A method as called for in claim 5, wherein said lignin and chloride
salt are added to said solvent and then said 2-propenamide and
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene chloride or
methylsulfate are added.
12. A method as called for in claim 11, wherein said hydroperoxide is
selected from the group consisting of t-butyl hydroperoxide and hydrogen
peroxide.
13. A method as set forth in claim 5, wherein said solvent comprises an
organic-water solvent mixture.
14. A method as called for in claim 4 further comprising increasing the
molecular weight of said copolymer during polymerization which comprises
effecting said polymerization in a reaction solvent which is a mixture of
water and an organic solvent to allow said reaction to proceed in a
gelated state.
15. The method according to claim 14, wherein said molecular weight is
increased to a molecular weight ranging from about 15,000 to about
30,000,000.
16. The method according to claim 14, wherein said reaction occurs at about
room temperature.
17. The method according to claim 14, wherein the amount of said solvent
ranges from about 10 to about 50 volume percent water, and from about 90
to about 50 volume percent organic solvent.
18. A method as called for in claim 4 wherein said copolymerizing step is
conducted utilizing from about zero molar percent to about 99 molar
percent of 2-propenamide, and from about one molar percent to about 100
molar percent of 2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene
chloride or methylsulfate.
19. A method as called for in claim 4 wherein said step of copolymerizing
comprises: adding from about 0.32 to about 3.0 weight percent lignin, from
about 0.0 to about 7.6 weight percent 2-propenamide, from about 0.1 to
11.0 weight percent of
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene with neutralizing
anion, from about 0.6 to about 15.3 weight percent calcium chloride, from
about 0.0 to about 6.1 weight percent aqueous solution of cerium (+IV),
and from about 60 to about 97 weight percent solvent.
20. A method as called for in claim 5 wherein said solvent is selected from
a group consisting of dimethyl sulfoxide, dimethyl acetamide, dimethyl
formamide, 1,4-dioxine, 1-methyl-2-pyrrolidianone and pyridine.
21. A method as called for in claim 5 wherein said solvent is a mixture of
at least one selected from the group consisting of dimethyl sulfoxide,
dimethyl acetamide, dimethyl formamide, 1,4-dioxane,
1-methyl-2-pyrrolidianone, pyridine and water.
22. A method as called for in claim 4 wherein said anion is selected from a
group consisting of chloride, methyl sulfate, bromide, nitrate and
bicarbonate.
23. A method as called for in claim 4 wherein said copolymerization is
allowed to proceed such that the total graft copolymer molecular weight is
in the range of about 15,000 to 30,000,000.
24. The method for preparing a complex polymer of lignin which comprises:
(a) adding a hydroperoxide to a solvent consisting of a mixture of fluids
of differing polarity such that the total solvent is highly effective in
dissolving monomers to be attached to the lignin; and
(b) adding lignin, a chloride-containing salt, 2-propenamide and
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene chloride or
methylsulfate to said solution, thereby initiating free radical
polymerization. |
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Claims  |
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Description  |
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FIELD OF THE INVENTION
The present invention relates to water-soluble graft copolymers of
lignin-(2-propenamide)-(2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-
1-ene chloride or methylsulfate), methods of making the same and uses
therefor.
BACKGROUND OF THE INVENTION
Aqueous solutions which flow at a controlled rate under a given shear
stress are required throughout a variety of industrial applications. Such
control of viscosity of water is achieved by adding to the water agents
such as clays, large amounts of polar organic compounds such as
polyacrylates or high concentrations of salts. These aqueous solutions
suspend finely divided solids and will flow slowly when exposed to shear
stress. Such solutions also flow more uniformly in situations where
numerous paths, providing different resistances to flow, are open to the
fluids.
However, each of these conventional agents has attendant disadvantages
particularly when used to recover oil from subterranean wells. The
application of these agents to flow control and
flocculation-deflocculation control requires careful adjustment of the
concentration of an active agent in the solution and control of adsorption
of the active agent onto suspended solids or the matrix of the porous
media. Such control is impossible when negatively charged agents are
introduced into systems containing positively-charged surfaces such as
calcite. The negatively-charged agents are completely adsorbed onto the
solid. Further, if the solution contains divalent cations, the
negatively-charged agents associate with the cations and precipitate.
Hence, a need continues to exist for new agents which are capable of
suitably thickening water and aqueous solutions to produce aqueous
solutions having the desirable properties as outlined below but which are
free of attendant disadvantages in the prior art agents.
SUMMARY OF THE INVENTION
A water-soluble graft copolymer of
lignin-(2-propenamide)-(2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-
1-ene chloride or methylsulfate) having a central lignin network and at
least one grafted side chain, R, having randomly repeating units of the
formulas:
##STR2##
such that the central lignin network has a molecular weight of about 1,000
to 150,000 and the total number of random units in the grafted side chain
or chains is in the range of 50 to 300,000 units, such that the total
copolymer molecular weight is in the range of 15,000 to 30,000,000. The
resulting molecule bears multiple positive charges.
Objects, features and advantages of the present invention are to provide a
positively-charged lignin graft copolymer; provide simplistic and reliable
processes for preparing such lignin graft copolymer; provide a method for
using a positively-charged lignin graft copolymer in preparing highly
viscous, aqueous solutions which are particularly useful in oil recovery
from subterranean wells into carbonate reservoirs; and to provide a method
of boosting or enhancing polymer molecular weights during polymerization
reactions.
DETAILED DESCRIPTION
In accordance with the present invention, there is provided a high
molecular weight graft copolymer containing lignin as the backbone network
and
poly((1-amidoethylene)-co-(1-methyl-1-(N5,N5-dimethyl-5-ammonium-1-oxo-2-o
xyhexyl) ethylene)) with appropriate counter ion as the grafted side chain.
Lignin [8068-00-6] is derived from woody plants. In fact, after cellulose,
it is the principal constituent of the woody structure of higher plants.
Lignin, which makes up about 25% of the weight of dry wood, acts as a
cementing agent to bind the matrix of cellulose fibers together into a
rigid woody structure. See Biochemistry by A. L. Lehninger (Worth
Publishers, 1970).
Moreover, lignin sources are abundant. Although the wood and bark waste
from the lumber industry and wastes from agricultural operations could
provide extremely large quantities of lignin, perhaps the most accessible,
albeit smaller, source is the pulp and paper industry. For example, for
1978, it has been estimated that the U.S. chemical-pulp industry produced
1.55.times.10.sup.7 metric tons of alkali lignin and 1.6.times.10.sup.6
tons of lignosulfonic acids. See Encyclopedia of Chemical Technology, vol.
14 (Kirk-Othmer, 1981).
In general, the molecular structure of the repeating lignin units and the
appropriate numbering thereof is as follows:
##STR3##
It appears that, regardless of origin, lignin [8068-00-6] is a complex,
oxyphenylpropene polymer. In the natural state, lignin is a highly
branched and partially cross-linked polymer. However, there appears to be
some structural variation in branching depending upon whether the lignin
is derived from coniferous or deciduous species or from bark, cambium,
sapwood or heartwood. During recovery, the lignin is chemically altered
and is available in relatively pure form as a derivative having a
molecular weight of about 1,000 to 150,000. Suitable lignins which may be
used according to the present invention are alkali lignins, HCl lignins,
milled wood lignins (MWL) and 1,4-dioxane lignins, for example.
Alkali lignins are used in the examples of this application. However,
reactions can be run on solvent-extracted lignin, kraft lignin, pine
lignin, aspen lignin and steam-exploded lignin. Alkali lignins are tan,
brown or black powders. When free of metal cations such as sodium or
potassium, alkali lignins are water-insoluble materials and are commonly
called "free acid" or "acid free" lignin. When containing metal cations,
such as sodium or potassium, the alkali lignins are slightly water soluble
materials which increase in water solubility as the pH increases from 7
toward 14 and become completely soluble in 5 wt. % aqueous sodium
hydroxide solutions. Alkali lignins have, as a basic repeating unit, the
oxyphenylpropyl unit:
##STR4##
The aromatic ring is often alkoxy substituted, as shown, and the propene
group often has a hydroxyl group attached in place of one hydrogen. Alkyl
groups appear on some of the aromatic groups of the polymer and sulfur may
be chemically bound to parts of the polymer, though few, if any, sulfonate
groups occur.
Bonding between repeat units in alkali lignin is complex and involves
carbon-carbon bonds between aromatic and/or alkyl carbons as well as ether
bonds between aromatic and/or alkyl carbons. Labile hydrogens exist in the
material and may be replaced by metal cations, such as sodium, potassium,
calcium, or ammonium ions, to form alkali lignin salts. Alkali lignins are
readily identified by method of production and are a familiar class of
compounds to those versed in the paper making art.
In accordance with the present invention, to the lignin macromolecule,
specifically to the oxyphenylpropene repeat unit, is grafted repeating
units of 1-amidoethylene:
##STR5##
in combination with positively-charged repeating units of
(1-methyl-1-(N5,N5,-dimethyl-5-ammonium-1-oxo-2-oxyhexyl) ethylene):
##STR6##
For example, when using alkali lignins in accordance with the present
invention, a lignin graft copolymer of the following formula is produced:
##STR7##
In this structural formula, the subscripts m and n are used to show that
large numbers of the repeating units can be attached to the lignin
backbone but the formula does not mean that these repeat units occur in
strings of one type followed by strings of another type. Usually, the
graft copolymers formed have random copolymer side chains with the two
repeat units occurring in random sequence in the chain.
The preparation of this copolymer is accomplished, in general, under
oxygen-free conditions by adding a redox initiator, a chloride salt,
2-propenamide, and 2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene
chloride or methylsulfate,
##STR8##
to a lignin dispersion in a suitable solvent and allowing time for graft
polymerization to occur.
Preparation of alkali
lignin-(2-propenamide)-(2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-
1-ene chloride or methylsulfate) graft copolymer in dimethylsulfoxide will
now be illustrated for a sample composed of between 0.32 and 3.0 weight
percent lignin, 1.2 and 7.6 weight percent 2-propenamide, 0.1 to 11.0
weight percent 2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene
(chloride or methylsulfate), 0.6 to 15.3 weight percent calcium chloride,
0.0 to 6.1 weight percent aqueous solution of cerium (+IV), and 60 to 97
weight percent solvent.
Significant variation in reaction mixture composition is possible as will
be illustrated in the examples to follow. The synthesis method for these
copolymers will now be described, generally.
As a suitable solvent for the graft copolymerization of the present
invention, it should be noted that, in general, organic solvents are used
and, of these, the polar, aprotic solvents are preferred. Particularly
noteworthy are the solvents dimethyl sulfoxide (DMSO), dimethyl acetamide
(DMAc), dimethyl formamide (DMF), 1,4-dioxane, 1-methyl-2-pyrrolidianone
and pyridine. Of course, mixtures of these solvents can also be used such
as 50/50 (vol/vol) mixtures of DMSO and 1,4-dioxane However, it is also
possible to use various mixtures of the above solvents, such as a 50/50
(vol/vol) mixture of DMSO with water.
An aliquot of about 20 mL of purified solvent is placed in a 125 mL conical
flask or stopperable test tube. Lignin and finely ground anhydrous calcium
chloride are added to the pure solvent and the mixture is stirred for
about 20 minutes while being bubbled with nitrogen. After 10 minutes of
nitrogen saturation, a hydroperoxide such as hydrogen peroxide or
2-hydroperoxy-1,4-dioxycyclohexane is added to the reaction mixture. This
addition can be made by adding an aqueous solution of the peroxide for
safe handling or the peroxide can be added directly. Solid 2-propenamide
and a nitrogen-saturated solution of
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene chloride or
methylsulfate in solvent are added while nitrogen gas is bubbled into the
mixture. After about 10 minutes, a sufficient volume of 0.05M ceric
sulfate in water may be added, the flask is sealed under nitrogen, and the
slurry is stirred for 10 more minutes. The reaction starts immediately.
The flask contents will often thicken slowly but may even solidify into a
precipitate-laden, viscous slurry.
The reaction flask is placed in a 30.degree. C. bath and allowed to sit for
two days The reaction is then terminated with 0.5 mL of 1 wt % of
hydroquinone in water. The reaction mixture is diluted with 100 mL of
water and stirred until a uniform reaction product is precipitated by
adding the dilute reaction mixture dropwise to 1 liter of 2-propanone or
other suitable nonsolvent for the graft copolymer. The solid is recovered
from 2-propanone by filtration and dried under vacuum at 40.degree. C. To
obtain a higher purity product which is more readily soluble, the reaction
product is recovered from nonsolvent by filtration and redissolved in
water. The same number of moles of disodium oxalate is added to the
product as there were moles of calcium chloride in the reaction mixture to
precipitate the calcium ion in the product. The aqueous solution with
precipitate is dialyzed against pure water using a
3,500-upper-molecular-weight-permeable, dialysis membrane for several
days. The polymer solution is centrifuged at 6000 rpm for 35 minutes to
sediment the precipitate and the supernate, pure polymer solution is
poured off. The aqueous solution containing the solid is then
freeze-dried.
It is preferred that all reagents used be of reagent grade purity but less
pure materials may be used if they do not contain inhibitors for the
reaction. Other concentrations of cerium (+IV) ion solution in other
nonreactive solvents can be used to add this reagent to the reaction and,
indeed, this reagent is not necessary for the reaction. The 0.05M cerium
(+IV) sulfate solution is stable and convenient to use. However, the
concentration of the ceric sulfate solution used can vary from about 0.01M
to 0.3M. Other reagents that may be used in place of a ceric ion
(Ce.sup.4+) include vanadium (V.sup.+5) or manganese ions
(Mn.sup.3+,Mn.sup.4+,Mn.sup.7+). It is preferred that the metal salt be
added as an aqueous solution. Moreover, ceric salts are a preferred
reagent for the graft polymerization. The reaction can be run without
adding cerium or other oxidizing metal ions but slightly higher yields and
better solubility properties are obtained when the oxidizing metal ion is
added. The graft copolymer can and will be produced if this reagent is not
added to the synthesis mixture but product properties are improved by the
addition of cerium (+4) solution. Other changes in this procedure, evident
to those skilled in synthesis or chemical manufacture can be made. The
graft copolymer can also be produced by adding nitrogen-saturated
2-propenamide to the reaction mixture in another solvent.
Other hydroperoxides, such as inorganic hydroperoxides or t-butyl
hydroperoxide, may be used in place of the hydrogen peroxide listed above.
The graft copolymerization reaction can be conducted with or without
stirring once the monomer and metal salt have been dispersed in the
reaction mixture. The reaction is allowed to proceed for 1 to 200 hours,
with 48 hours being a typical reaction time. It is preferred to terminate
the copolymerization by addition of a free radical scavenger such as
hydroquinone.
The graft terpolymer is easily recovered from a liquid reaction mixture. If
the reaction mixture is a gel or thick slurry, it can be made pourable by
mixing therewith 1 to 3 times its volume of distilled or deionized water
under low shear conditions until a homogeneous, pourable system is formed.
The reaction mixture is added to 2-20, preferably 5-10, times its volume
of a nonsolvent for the polymer, such as 2-propanone. Preferably the
nonsolvent is stirred vigorously so as to form a vortex and the copolymer
solution is slowly drained directly into the center of this vortex. The
precipitated graft copolymer is then removed from the nonsolvent solution
by filtration, washed with nonsolvent, filtered, and vacuum-dried to a
constant weight. A purer product can be obtained by the dialysis-freeze
drying process described above.
The following examples illustrate certain embodiments of this invention
wherein parts and percentages are by weight and temperatures are in
centigrade unless otherwise indicated. Indulin AT, a commercial lignin
product of the Westvaco Corporation, and Eastman reageat-grade
2-propenamide were used in these synthesis. The compound
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene chloride was
obtained from Alcolac Specialty Chemicals of 3440 Fairfield Road,
Baltimore, Md. 21226, as a 75 weight percent solution in water. It was
purified by freeze drying to remove water and recrystallized from
ethanol-(2-propanone)(20:80 mixture by volume). The purified crystals were
dried under vacuum and stored in a freezer. The compound
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene methylsulfate was
obtained from CPS Chemical Company, Inc., of P.O. Box 162, Old Bridge,
N.J. 08857, as an 80 weight percent solution in water. It was purified by
freeze drying to remove water and recrystallized from
ethanol-(2-propanone)(20:80 mixture by volume). The purified crystals were
dried under vacuum and stored in a freezer. Paradioxane and dimethyl
sulfoxide, of reagent grade, from Mallinckrodt Chemical Company and
anhydrous calcium chloride also therefrom were used in these examples.
Ceric sulfate solution was prepared from reagent grade ceric sulfate and
distilled water. The hydroquinone solution was 1 wt % hydroquinone in
distilled water. The limiting viscosity number of the product in pure
water was determined using the Fuoss equation (a) to extrapolate several
viscosity measurements, .eta., to zero polymer concentration.
C/.eta..sub.sp =1/[.eta.]+Q.sub.f C.sup.1/2
Here .eta..sub.sp =(.eta.-.eta.o)/.eta..sub.o, C is polymer concentration
in g/dL, Q.sub.f is a fitting constant, and [.eta.] is limiting viscosity
number. See J. Poly. Sci., 3,603-604 (1948).
The present invention will now be further illustrated by certain examples
and references which are provided for purposes of illustration only and
are not intended to limit the present invention.
Yield was calculated from the formula: (g=grams)
##EQU1##
EXAMPLES
Example 1
A total of 0.5 g of lignin and 0.38 g of calcium chloride were placed in a
125 mL test tube containing 20.0 g of dimethylsulfoxide. The mixture was
stir-bubbled with nitrogen (N.sub.2) for about 2 minutes before 0.50 mL of
30 percent, aqueous hydrogen peroxide was added to the reaction mixture.
N.sub.2 was bubbled through the reaction mixture for about 2 more minutes,
the system was stirred for about 20 minutes, and 1.40 g of 2-propenamide
(I) was then added. After about 2 minutes of stirring and N.sub.2
bubbling, 1.18 g of 2-propenamide (I) and 1.94 g of
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene chloride (II) in
11.08 g of dimethylsulfoxide were added. After 10 minutes of stirring and
bubbling N.sub.2 through the reaction mixture, the flask was stoppered and
placed in a 30.degree. C. bath for 2 days. The mole ratio of monomer I to
II in the reaction solution was 4 to 1. The chloride content of the
reaction mixture was 1.554 weight percent. The reaction was then
terminated by adding 0.5 mL of 1% hydroquinone and 100 mL of water
thereto. The stirred reaction mixture was precipitated in 1/2 L of
2-propanone and recovered by filtration. The recovered solid was dissolved
in 100 mL of water and 0.46 g of disodium oxalate was added to the produce
to precipitate the calcium ion in the product. The aqueous solution with
precipitate was dialyzed against pure water using a
3,500-upper-molecular-weight-permeable, dialysis membrane from 3 days. The
polymer solution was centrifuged at 6000 rpm for 35 minutes to sediment
the precipitate and the supernate, pure polymer solution was poured off.
The dilute reaction product from the dialysis tube was recovered by freeze
drying and found to weigh 4.59 g. The product was labeled 24-136-1.
Yield=91.43 wt %. The nitrogen content of the product was 11.62 weight
percent. Limiting viscosity number, [.eta.], of the product was 13.07
dL/g.
Example 2
A total of 0.5 g of lignin and 0.26 g of calcium chloride were placed in a
125 mL test tube containing 20.0 g of dimethylsulfoxide. The mixture was
stir-bubbled with nitrogen (N.sub.2) for about 2 minutes before 0.50 mL of
30 percent, aqueous hydrogen peroxide were added to the reaction mixture.
N.sub.2 was bubbled through the reaction mixture for about 2 more minutes,
the system was stirred for about 20 minutes, and 1.40 g of 2propenamide
(I) was then added. After about 2 minutes of stirring and N.sub.2
bubbling, 0.85 g of 2-propenamide (I) and 2.82 g of
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene chloride (II) in
14.82 g of dimethylsulfoxide were added. After about 10 minutes of
stirring and bubbling N.sub.2 through the reaction mixture, the flask was
stoppered and placed in a 30.degree. C. bath for 2 days. The mole ratio of
monomer I to II in the reaction solution was 7 to 3. The chloride content
of the reaction mixture was 1.570 weight percent. The reaction was then
terminated by adding 0.5 mL of 1% hydroquinone and 100 mL of water
thereto. The stirred reaction mixture was precipitated in 1/2 L of
2-propanone and recovered by filtration. The recovered solid was dissolved
in 100 mL of water and 0.32 g of disodium oxalate was added to the product
to precipitate the calcium ion in the product. The aqueous solution with
precipitate was dialyzed against pure water for 3 days. The polymer
solution was centrifuged at 6000 rpm for 35 minutes to sediment the
precipitate and the supernate, pure polymer solution was poured off. The
dilute reaction product from the dialysis tube was recovered by freeze
drying and found to weight 5.24 g. The product was labeled 24-136-2.
Yield=94.07 wt %. The nitrogen content of the product was 10.36 weight
percent. Limiting viscosity number, [.eta.], of the product was 16.07
dL/g.
Example 3
A total of 0.5 g of lignin and 0.11 g of calcium chloride were placed in a
125 mL test tube containing 20.0 g of dimethylsulfoxide. The mixture was
stir-bubbled with nitrogen (N.sub.2) for about 2 minutes before 0.50 mL of
30 percent, aqueous hydrogen peroxide was added to the reaction mixture.
N.sub.2 was bubbled through the reaction mixture for about 2 more minutes,
the system was stirred for about 20 minutes, and 1.41 g of 2propenamide
(I) was then added. After about 2 minutes of stirring and N.sub.2
bubbling, 0.52 g of 2-propenamide (I) and 3.73 g of
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene chloride (II) in
19.40 g of dimethylsulfoxide were added. After about 10 minutes of
stirring and bubbling N.sub.2 through the reaction mixture, the flask was
stoppered and placed in a 30.degree. C. bath for 2 days. The mole ratio of
monomer I to II in the reaction solution was 3 to 2. The chloride content
of the reaction mixture was 1.534 weight percent. The reaction was then
terminated by adding 0.5 mL of 1% hydroquinone and 100 mL of water
thereto. The stirred reaction mixture was precipitated in 1/2 L of
2-propanone and recovered by filtration. The recovered solid was dissolved
in 100 mL of water and 0.13 g of disodium oxalate was added to the product
to precipitate the calcium ion in the product. The aqueous solution with
precipitate was dialyzed against pure water for 3 days. The polymer
solution was centrifuged at 6000 rpm for 35 minutes to sediment the
precipitate and the supernate, pure polymer solution was poured off. The
dilute reaction product from the dialysis tube was recovered by freeze
drying and found to weigh 5.62 g. The product was labeled 24-136-3.
Yield=91.23 wt %. The nitrogen content of the product as 9.09 weight
percent. Limiting viscosity number, [.eta.], of the product was 39.84
dL/g.
Example 4
A total of 0.5 g of lignin and 0.01 g of calcium chloride were placed in a
125 mL test tube containing 20.0 g of dimethylsulfoxide. The mixture was
stir-bubbled with nitrogen (N.sub.2) for about 2 minutes before 0.50 mL of
30 percent, aqueous hydrogen peroxide was added to the reaction mixture.
N.sub.2 was bubbled through the reaction mixture for about 2 more minutes,
the system was stirred for about 20 minutes, and 1.40 g of 2-propenamide
(I) was then added. After about 2 minutes of stirring and N.sub.2
bubbling, 0.21 g of 2-propenamide (I) and 4.67 g of
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene chloride (II) in
25.31 g of dimethylsulfoxide were added. After about 10 minutes of
stirring and bubbling N.sub.2 through the reaction mixture, the flask was
stoppered and placed in a 30.degree. C. bath for 2 days. The mole ratio of
monomer I to II in the reaction mixture was 1 to 1. The chloride content
of the reaction mixture was 1.530 weight percent. The reaction was then
terminated by adding 0.5 mL of 1% hydroquinone and 100 mL of water
thereto. The stirred reaction mixture was precipitated in 1/2 L of
2-propanone and recovered by filtration. The recovered solid was dissolved
in 100 mL of water and 0.01 g of disodium oxalate was added to the product
to precipitate the calcium ion in the product. The aqueous solution with
precipitate was dialyzed against pure water for 3 days. The polymer
solution was centrifuged and the supernate, pure polymer solution was
poured off. The dilute reaction product from the dialysis tube was
recovered by freeze drying and found to weigh 6.15 g. The product was
labeled 24-136-4. Yield=90.71 wt %. The nitrogen content of the product
was 7.76 weight percent. Limiting viscosity number, [.eta.], of the
product was 39.85 dL/g.
Note that these four examples, numbers 1 to 4, show that different mole
ratios of monomers can be used to produce product in yields in excess of
90 weight percent if the chloride ion content of the reaction mixture is
maintained at between 1.53 and 1.57 weight percent. This optimum chloride
ion content must be found for a given solvent system by experimental
tests. It is maintained by lowering the amount of calcium chloride added
to the reaction to compensate for the amount of chloride ion contained in
the positively charged monomer.
Example 5
A total of 0.51 g of lignin and 0.88 g of calcium chloride were placed in a
125 mL test tube containing 10.0 g of dimethylsulfoxide. The mixture was
stir-bubbled with nitrogen (N.sub.2) for about 2 minutes before 0.50 mL of
30 percent, aqueous hydrogen peroxide was added to the reaction mixture.
N.sub.2 was bubbled through the reaction mixture for about 2 more minutes,
the system was stirred for about 20 minutes, and 1.39 g of 2propenamide
(I) in 10.0 g of dimethylsulfoxide was then added. After about 2 minutes
of stirring and N.sub.2 bubbling, 1.17 g of 2-propenamide (I) and 2.55 g
of 2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene methylsulfate
(II) in 10.08 g of dimethylsulfoxide were added. After 10 minutes of
stirring and bubbling N.sub.2 through the reaction mixture, the flask was
stoppered and placed in a 30.degree. C. bath for 2 days. The mole ratio of
monomer I to II in the reaction solution was 4 to 1. The chloride content
of the reaction mixture was 1.519 weight percent. The solids content of
the reaction mixture was 18.89 weight percent. The reaction was then
terminated by adding 0.5 mL of 1% hydroquinone and 100 mL of water
thereto. The stirred reaction mixture was precipitated in 1/2 L of
2-propanone and recovered by filtration. The recovered solid was dissolved
in 100 mL of water and 1.06 g of disodium oxalate was added to the product
to precipitate the calcium ion in the product. The aqueous solution with
precipitate was dialyzed against pure water using a
3,500-upper-molecular-weight-permeable, dialysis membrane for 3 days. The
polymer solution was centrifuged at 6000 rpm for 35 minutes to sediment
the precipitate and the supernate, pure polymer solution was poured off.
The dilute reaction product from the dialysis tube was recovered by freeze
drying and found to weigh 4.34 g. The product was labeled 24-139-1.
Yield=77.22 wt %. Limiting viscosity number, [.eta.], of the product was
5.07 dL/g.
Example 6
A total of 0.50 g of lignin and 0.93 g of calcium chloride were placed in a
125 mL test tube containing 10.0 g of dimethylsulfoxide. The mixture was
stir-bubbled with nitrogen (N.sub.2) for about 2 minutes before 0.50 mL of
30 percent, aqueous hydrogen peroxide were added to the reaction mixture.
N.sub.2 was bubbled through the reaction mixture for about 2 more minutes,
the system was stirred for about 20 minutes, and 1.39 g of 2-propenamide
(I) in 10.0 g of dimethylsulfoxide was then added. After about 2 minutes
of stirring and N.sub.2 bubbling, 0.53 g of 2-propenamide (I) and 5.15 g
of 2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene methylsulfate
(II) in 10.72 g of dimethylsulfoxide were added. After 10 minutes of
stirring and bubbling N.sub.2 through the reaction mixture, the flask was
stoppered and placed in a 30.degree. C. bath for 2 days. The mole ratio of
monomer I to II in the reaction solution was 3 to 2. The chloride content
of the reaction mixture was 1.500 weight percent. The calcium chloride
content was 2.34 weight percent. The solids content of the reaction
mixture was 22.66 weight percent. The reaction was then terminated by
adding 0.5 mL of 1% hydroquinone and 100 mL of water thereto. The stirred
reaction mixture was precipitated in 1/2 L of 2-propanone and recovered by
filtration. The recovered solid was dissolved in 100 mL of water and 1.12
g of disodium oxalate was added to the product to precipitate the calcium
ion in the product. The aqueous solution with precipitate was dialyzed
against water for 3 days. The polymer solution was centrifuged at 6000 rpm
for 35 minutes to sediment the precipitate and the supernate, pure polymer
solution was poured off. The dilute reaction product from the
centrifugation was recovered by freeze drying and found to weigh 6.07 g.
The product was labeled 24-139-2. Yield=80.18 wt %. Limiting viscosity
number, [.eta.], of the product was 23.41 dL.
Example 7
A total of 0.50 g of lignin and 0.99 g of calcium chloride were placed in a
125 mL test tube containing 10.0 g of dimethylsulfoxide. The mixture was
stir-bubbled with nitrogen (N.sub.2) for about 2 minutes before 0.50 mL of
30 percent, aqueous hydrogen peroxide was added to the reaction mixture.
N.sub.2 was bubbled through the reaction mixture for about 5 more minutes.
Then 1.29 g of 2-propenamide (I) and 8.36 g of
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene methylsulfate (II)
in 19.28 g of dimethylsulfoxide were added. After 10 minutes of stirring
and bubbling N.sub.2 through the reaction mixture, the flask was stoppered
and placed in a 30.degree. C. bath for 2 days. The mole ratio of monomer I
to II in the reaction solution was 2 to 3. The chloride content of the
reaction mixture was 1.547 weight percent. The calcium chloride content
was 2.42 weight percent. The solids content of the reaction mixture was
28.45 weight percent. The reaction was then terminated by adding 0.5 mL of
1% hydroquinone and 100 mL of water thereto. The stirred reaction mixture
was precipitated in 1/2 L of 2-propanone and recovered by filtration. The
recovered solid was dissolved in 100 mL of water and 1.19 g of disodium
oxalate was added to the product to precipitate the calcium ion in the
product. The aqueous solution with precipitate was dialyzed against water
for 3 days. The polymer solution was centrifuged to sediment the
precipitate and the supernate, pure polymer solution was poured off. The
dilute reaction product from the centrifugation was recovered by freeze
drying and found to weigh 7.15 g. The product was labeled 24-139-3.
Yield=70.44 wt %. Limiting viscosity number, [.eta.], of the product was
41.73 dL/g.
Example 8
A total of 0.50 g of lignin and 1.02 g of calcium chloride were placed in a
125 mL test tube containing 10.0 g of dimethylsulfoxide. The mixture was
stir-bubbled with nitrogen (N.sub.2) for about 2 minutes before 0.50 mL of
30 percent, aqueous hydrogen peroxide was added to the reaction mixture.
N.sub.2 was bubbled through the reaction mixture for about 5 more minutes.
Then 0.64 g of 2-propenamide (I) and 10.21 g of
2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene methylsulfate (II)
in 21.40 g of dimethylsulfoxide were added. After 10 minutes of stirring
and bubbling N.sub.2 through the reaction mixture, the flask was stoppered
and placed in a 30.degree. C. bath for 2 days. The mole ratio of monomer I
to II in the reaction solution was 1 to 4. The chloride content of the
reaction mixture was 1.474 weight percent. The calcium chloride content
was 2.304 weight percent. The solids content of the reaction mixture was
29.07 weight percent. The reaction was then terminated by adding 0.5 mL of
1% hydroquinone and 100 mL of water thereto. The stirred reaction mixture
was precipitated in 1/2 L of 2-propanone and recovered by filtration. The
recovered solid was dissolved in 100 mL of water and 1.23 g of disodium
oxalate was added to the product to precipitate the calcium ion in the
product. The aqueous solution with precipitate was dialyzed against water
for 3 days. The polymer solution was centrifuged to sediment the
precipitate and the supernate, pure polymer solution was poured off. The
dilute reaction product from the centrifugation was recovered by freeze
drying and found to weigh 10.33 g. The product was labeled 24-139-4.
Yield=91.40 wt %. Limiting viscosity number, [.eta.], of the product was
55.03 dL/g.
Note that these reactions, examples 5 to 8, yield more than 80 weight
percent product but yields are not as high as those of examples 1 to 4.
Thus, these reactions, while not run at an optimum concentration of
chloride ion in the reaction mixture, still produce a large yield of graft
polymer. Further, these products also have different amounts of charged
and uncharged repeat units in the product and that difference is produced
by varying the monomer ratio between the two repeat units.
Example 9
A total of 0.50 g of lignin and 1.07 g of calcium chloride were placed in a
125 mL test tube containing 10.0 g of dimethylsulfoxide. The mixture was
stir-bubbled with nitrogen (N.sub.2) for about 2 minutes before 0.50 mL of
30 percent, aqueous hydrogen peroxide was added to the reaction mixture.
N.sub.2 was bubbled through the reaction mixture for about 5 more minutes.
Then 12.77 g of 2-methyl-N7,N7-dimethyl-7-ammonium-3-oxo-4-oxyoct-1-ene
methylsulfate (II) in 21.40 g of dimethylsulfoxide was added. After 10
minutes of stirring and bubbling N.sub.2 through the reaction mixture, the
flask was stoppered and placed in a 30.degree. C. bath for 2 days. The
mole ratio of monomer I to II in the reaction solution was 0 to 100. This
sample utilized only II monomer to form
poly(lignin-g-(1-methyl-1-(N5,N5-dimethyl-5-ammonium-1-oxo-2-oxyhexyl)ethy
lene methylsulfate)), a graft copolymer with a one repeat unit sidechain.
The chloride content of the reaction mixture was 1.503 weight percent. The
calcium chloride content was 2.350 weight percent. The solids content of
the reaction mixture was 32.58 weight percent. The reaction was then
terminated by adding 0.5 mL of 1% hydroquinone and 100 mL of water
thereto. The stirred reaction mixture was precipitated in 1/2 L of
2-propanone and recovered by filtration. The recovered solid was dissolved
in 100 mL of water and 1.29 g of disodium oxalate was added to the product
to precipitate the calcium ion in the product. The aqueous solution with
precipitate was dialyzed against water for 3 days. The polymer solution
was centrifuged to sediment the precipitate and the supernate, pure
polymer solution was poured off. The dilute reaction product from the
centrifugation was recovered by freeze drying and found to weigh 9.40 g.
The product was labeled 24-139-5. Yield=70.91 wt %. Limiting viscosity
number, [.eta.], of the product was 85.64 dL/g.
The product of Example 9 is
poly(lignin-co-(1-methyl-1-(N5,N5-dimethyl-5-ammonium-1-oxo-2-oxyhexyl)
ethylene)), a graft copolymer with all charged repeat units in the
sidechain.
The data of the following Table I shows that the products of this invention
are effective viscosifiers for water.
TABLE 1
__________________________________________________________________________
Viscosities of Aqueous
Solutions of Graft Terpolymer
*Viscosity when product concentration in water
Product from
Sample
is (wt %):
Example Number
Number
1.0 0.298
0.199
0.0997
0.050
__________________________________________________________________________
9 24-139-5
-- 5.115
4.373
3.182
2.323
0.300
0.197
0.1003
0.0501
0.025 0.0099
8 24-139-4
4.424
3.618
2.749
2.013
1.481 1.108
0.1 0.0747
0.037
0.015
0.0099
7 24-139-3
1.904
1.918
1.501
1.134
1.019
0.102
0.0597
0.030
0.0100
6 24-139-2
1.557
1.321
1.113
0.923
0.298
0.154
0.102
0.0703
5 24-139-1
1.413
1.166
1.057
0.958
1.0 0.322
0.165
0.0997
0.0502
4 24-136-4
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