US3885069A - Preparation of crosslinked polyethylenimine and impregnation of cellulosic material with in situ crosslink-polymerized ethylenimine - Google Patents
Preparation of crosslinked polyethylenimine and impregnation of cellulosic material with in situ crosslink-polymerized ethylenimine Download PDFInfo
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- US3885069A US3885069A US279919A US27991972A US3885069A US 3885069 A US3885069 A US 3885069A US 279919 A US279919 A US 279919A US 27991972 A US27991972 A US 27991972A US 3885069 A US3885069 A US 3885069A
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M13/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
- D06M13/322—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with compounds containing nitrogen
- D06M13/487—Aziridinylphosphines; Aziridinylphosphine-oxides or sulfides; Carbonylaziridinyl or carbonylbisaziridinyl compounds; Sulfonylaziridinyl or sulfonylbisaziridinyl compounds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J39/00—Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/08—Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/16—Organic material
- B01J39/18—Macromolecular compounds
- B01J39/22—Cellulose or wood; Derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M15/00—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
- D06M15/19—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
- D06M15/37—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D06M15/61—Polyamines polyimines
Definitions
- This invention relates to chemical treatment of cotton and other fibrous materials. Specifically, this invention relates to the deposition of in situ formed ethylenimine network polyer in fibrous materials. This is accomplished by impregnation of the substrate with ethylenimine prepolymer prepared by reacting ethylenimine with a difunctional or polyfunctional alkyl or aryl halide.
- the products of the present process normally have a low ion-exchange capacity while having a high capacity for complexing with heavy metals, such as mercury for example.
- This invention should be a very useful tool in this era of emphasis on Ecology, its problems and solutions.
- the main object of this invention is to provide an improved method for the in situ formation of ethylenimine network polymer in the interstaces of porous or absorbent materials.
- Another object of this invention is to provide an ionexchange material for acidic substances.
- a third object of this invention is to provide a good scavenger of heavy metals to reduce pollution in water.
- a fourth object of this invention is to provide a means for imparting a rot and weather resistance to cotton and other cellulose textiles.
- diand polyhalogenated organic compounds other than that illustrated by the use of 1,2- dichloroethane, have been employed in the investigative work which led to the process of this inventiion, as initiators and crosslinking agents in the polymerization of ethylenimine.
- the molar ratio of ethylenimine to diand polyhalogenated compounds is about from 44:1 to 27:1.
- the polymerization of ethylenimine must be conducted cautiously with efficient removal of heat to avoid violent and possibly explosive reactions. Polymerization conducted as disclosed in this specification can proceed without incident.
- the add-on is controlled by the concentration of prepolymer in the pad bath. Add-ons of 50 percent were achieved readily in the process of investigation. Little or no grafting or crosslinking of the cellulose occurred during curing, as evidenced by the solubility of the cellulose in a standard Cuene solution (copperethylenediamine hydroxide). The ethylenimine network polymer was insoluble in the Cuene and remained visible after the cellulose had dissolved. The polymer is apparently held onto the cotton cellulose by virtue of its insolubility and by hydrogen-bonding and entanglement with the cotton fibers.
- crosslinked polymer When the crosslinked polymer is prepared separately it is clear, firm and flexible, it can be broken readily, and is insoluble in water, acids, and strong solutions of base as well as in all organic solvents tested. Under certain conditions the polymer alone will disintegrate to a coarse insoluble powder. The extent of this effect decreases with age of the polymer.
- impregnated fabrics have shown a high capacity for complexing certain heavy metals.
- capacity of impregnated fabric to complex mercury since mercury is one of the more undesirable contaminants in water. It has been visulized that these fibrous materials can well serve to remove many irritants from the air upon being used as filtering devices. Exploratory investigations indicate further value of the fibrous materials prepared by the process of this invention, i.e., rot and mildew resistance can be imparted by the implementation of the process.
- EXAMPLE 1 Eight different samples for the formation of the prepolymer are shown in the following table (Table l). The proportion of halide to ethylenimine may be varied as desired but the most useful and easily controlled molar proportion is that set forth in Sample 5. The temperature' in all cases must be controlled within the range of about to 50C in order to prevent the reaction from becoming violent. When the prepolymer is formed (in about 16 hours when the temperature is kept at about C) it is ready for use in preparing padding solutions.
- the prepolymer When the prepolymer is dissolved in a solvent such as alcohol or water to form about 5% to percent solution, it is tabled for several days but when applied to fabric at a wet pickup of about from 50 percent to 150 percent and the solvent is allowed to evaporate a polymer network is formed within the cotton or other fibrous structure to which it is applied.
- a solvent such as alcohol or water
- Thls table only shows the halides that were tested as inltiaters for prepolymer preparation and crosslinking of ethylenimine.
- a swatch of cotton printcloth weighing 17.8 grams was treated with a 5 percent w/w solution of the propo- 5 lymer of Example 2 in ethanol, to a wet pickup of percent.
- the wet impregnated fabric was hung on a line and left unmolested at room temperature 25C) for 16 hours. It was then washed in flowing tap water for about 30 minutes and again hung to dry for another 16 hours at room temperature. When the fabric was removed from the drying line it was dry and it was evaluated for weight gain and nitrogen content.
- the weight gain (add-on) was 5 percent and the nitrogen content was 1.6 percent.
- Example 4 Repeating the processing of Example 4 and employing the same quantities and values therein, it was observed that the results were identical, when water was used as a solvent.
- EXAMPLE 6 IMPREGNATION OF COTTON SUBSTRATE (to produce in sity formed ethylenimine network polymer employing a tris(2-chloroethyl)phosphoramide with ethanol as solvent):
- a swatch of cotton printcloth weight 17.6 grams was treated with a percent w/w ethanolic solution of prepolymer which was prepared as described in Example 3.
- the wet pickup was 115 percent.
- the wet impregnated fabric was hung on a line and left unmolested at room temperature (C) for 16 hours. It was the washed in flowing distilled water for about minutes and again hung to dry for another 16 hours at room temperature. When the fabric was removed from the drying line it was dry. It was then evaluated for weight gain, nitrogen and phosphorus content, and overall appearance.
- the weight gain (add-on) was 15.8 percent.
- the nitrogen content was 3.62 percent and the phosphorous content was 0.32 percent.
- EXAMPLE 7 EXAMPLE 8 USE OF POLYMER AS SCAVENGER Mercury forms a complex with the network polymer which was formed in situ in the structure of cotton fabric.
- the network polymer formed in situ by the process of Example 4 was soaked for 1 hour in a 2.0 percent w/w solution of mercuric chloride. The fabric was then removed from the solution and washed with flowing distilled water. The washed fabric was allowed to air dry at room temperature and chemically analyzed. The mercury content was 3.45 percent.
- EXAMPLE 9 USE OF POLYMER AS SCAVENGER Mercury complexed with a network polymer which was formed The process of Example 8 was employed with the fabric of Example 6. The finished fabric contained 3.71 percent mercury.
- EXAMPLE 10 USE OF POROUS PAPER AS A SUBSTRATE A porous paper towel was processed in the same manner and using the same chemical mixture of Example 2. The add-on was 48 percent, after washing, and the nitrogen content was 7.29 percent.
- EXAMPLE 11 USE OF PEANUT SHELLS AS SUBSTRATE A quantity of peanut shells was ground to pass a 20 mesh screen and 26 grams were impregnated by soaking in a 20 percent solution of the prepolymer of Example 2. The shells were collected on a sintered glass filter and air was pulled through until the wet pickup was percent. The wet impregnated peanut shells were then allowed to dry in an open dish for 16 hours at 25C and suspended in water, then collected on a filter and washed with distilled water 10 times. The shells were then allowed to air dry and then evaluated. The add-on was 38 percent and the nitrogen content was 5.25 percent.
- a method for producing in situ formed, crosslinked polyethylenimine in a fibrous material comprising:
- ethylenimine with an alkyl halide selected from the group consisting of 1,2-dichloroethane. tris( 2-chloroethyl)phosphoramide, bis( 2-chloroethylinyl )-phosphonate, tris( 2.3- dibromopropyl)phosphate, tris( 1,3- dichloroisopropyl)phosphate, B,B'-dichloroethyl ether and dichloromethane in a molar ratio of about from 44:1 to 27:1;
- step (c) impregnating the fibrous material with the prepolymer of step (c) to obtain a wet pickup of about from 50 to percent;
- alkyl halide is selected from the group consisting of bis(2- chloroethylvinyl)phosphonate, tris (2,3- dibromopropyl)-phosphate and tris( 1,3- dichloroisopropyl)phosphate.
- alkyl halide is selected from the group consisting of 1,2- dichloroethane, dichloromethane and B,B- dichloroethyl ether.
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- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Textile Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Analytical Chemistry (AREA)
- Wood Science & Technology (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Abstract
Cotton and other fibrous material is impregnated with ethylenimine prepolymer prepared by reacting ethylenimine and certain di- and polyfunctional alkyl or aryl halide to produce an insoluble in situ formed network polymer which is physically bound in the structure of the substrate used. This new material is an excellent scavenger of heavy metals in water. This material can be prepared to be simultaneously low in ion-exchange capacity while being high in capacity for complexing with heavy metals.
Description
United States Patent Roberts et al.
[4 1 May 20, 1975 PREPARATION OF CROSSLINKED POLYETHYLENIMINE AND IMPREGNATION OF CELLULOSIC MATERIAL WITH IN SITU CROSSLINK-POLYMERIZED ETHYLENIMINE Inventors: Earl J. Roberts; Stanley P. Rowland, both of New Orleans, La.
The United States of America as represented by the Secretary of Agriculture, Washington, DC.
Filed: Aug. 11, 1972 Appl. No.: 279,919
Assignee:
US. Cl 427/396; 427/445; 210/36; 210/38; 260/2 EN Int. Cl.. C02b l/46; D06m 13/48; D06m 15/12 Field of Search 117/143 A, 140 A; 210/36, 210/38; 260/2 EN References Cited UNITED STATES PATENTS 2/1942 Ulrich 260/2 X 2,656,241 Drake et a]. 260/231 X 2,972,606 2/1961 Hartman et al.... 260/231 3,565,679 2/1971 Strother 117/143 X 3,671,304 6/1972 Mischutin ll7/l43 X OTHER PUBLICATIONS Segal et al., article in Textile Research Journal, Sept. 1963, pp. 739-745.
Primary Examiner-Mayer Weinblatt Assistant Examiner--Dennis L. Albrecht Attorney, Agent, or FirmM. Howard Silverstein; Max D. Hensley [5 7] ABSTRACT 5 Claims, No Drawings PREPARATION OF CROSSLINKED POLYETHYLENIMINE AND IMPREGNATION OF CELLULOSIC MATERIAL WITH IN SITU CROSSLINK-POLYMERIZED ETHYLENIMINE A non-exclusive, irrevocable, royalty-free license in the invention herein described throughout the world for all purposes of the United States Government, with the power to grant sublicences for such purposes. is hereby granted to the Government of the United States of America.
This invention relates to chemical treatment of cotton and other fibrous materials. Specifically, this invention relates to the deposition of in situ formed ethylenimine network polyer in fibrous materials. This is accomplished by impregnation of the substrate with ethylenimine prepolymer prepared by reacting ethylenimine with a difunctional or polyfunctional alkyl or aryl halide. The products of the present process normally have a low ion-exchange capacity while having a high capacity for complexing with heavy metals, such as mercury for example.
This invention should be a very useful tool in this era of emphasis on Ecology, its problems and solutions.
The main object of this invention is to provide an improved method for the in situ formation of ethylenimine network polymer in the interstaces of porous or absorbent materials.
Another object of this invention is to provide an ionexchange material for acidic substances.
A third object of this invention is to provide a good scavenger of heavy metals to reduce pollution in water.
A fourth object of this invention is to provide a means for imparting a rot and weather resistance to cotton and other cellulose textiles.
THE PRIOR ART Several researchers have dealt with various organic chemicals to obtain cotton derivatives with suitable ion-exchange capacity. Drake et al. have disclosed (U.S. Pat. NO. 2,656,251) the polymerization of ethylenimine with cotton fibers to produce ionexchange textiles; however, the disadvantage to the Drake process is that the polyethylenimine is not crosslinked nor covalently bonded to the cotton but is believed to be held onto the cotton by hydrogen bonding, since it is slowly lost upon repeated use and regeneration.
More recent investigations have indicated that although amine-containing cottons do have good ionexchange properties they generally have low capacity. It has also been determined that some aminecontaining cotton do form stable complexes with most heavy metals. The chief problem encountered with amine-containing cottons in which the amine bearing groups are covalently linked to the cellulose molecule is the requirement of multiple treatments in order to be able to attain a sufficiently high degree of add-on. It has been found necessary to crosslink the cotton first to prevent solubilization and dispersion of the cellulose at high levels of add-on.
An equation which can be used to illustrate an applicable case with reference to the chemistry of the present invention is the case where ethylenimine is reacted with 1,2-dichloroethane, thusly:
A variety of diand polyhalogenated organic compounds, other than that illustrated by the use of 1,2- dichloroethane, have been employed in the investigative work which led to the process of this inventiion, as initiators and crosslinking agents in the polymerization of ethylenimine. The molar ratio of ethylenimine to diand polyhalogenated compounds is about from 44:1 to 27:1. The polymerization of ethylenimine must be conducted cautiously with efficient removal of heat to avoid violent and possibly explosive reactions. Polymerization conducted as disclosed in this specification can proceed without incident.
When the prepolymer is allowed to age at room temperature curing occurs and is complete within about 16 hours; however, solutions of the prepolymer in ethanol or water are stable for several days. Curing begins when the solvent is allowed to evaporate.
With respect to preparation of cotton fabric containing crosslinked polyethylenimine formed in situ the add-on is controlled by the concentration of prepolymer in the pad bath. Add-ons of 50 percent were achieved readily in the process of investigation. Little or no grafting or crosslinking of the cellulose occurred during curing, as evidenced by the solubility of the cellulose in a standard Cuene solution (copperethylenediamine hydroxide). The ethylenimine network polymer was insoluble in the Cuene and remained visible after the cellulose had dissolved. The polymer is apparently held onto the cotton cellulose by virtue of its insolubility and by hydrogen-bonding and entanglement with the cotton fibers.
When the crosslinked polymer is prepared separately it is clear, firm and flexible, it can be broken readily, and is insoluble in water, acids, and strong solutions of base as well as in all organic solvents tested. Under certain conditions the polymer alone will disintegrate to a coarse insoluble powder. The extent of this effect decreases with age of the polymer.
The ion-exchange and complexing capacities of fabric impregnated with the polymer to several levels of add-on are presented in tabulated form to point out the most serviceable facets of the invention; however, a more complete report can be obtained in a paper by these inventors which appeared in Textile Research Journal in Oct. 1971, bearing the title Ion-Exchange and Complexing Properties of Cotton Fabric Containing Ethylenimine Network Polymer Formed in situ (see Vol. 41, pp 864-867).
The impregnated fabrics have shown a high capacity for complexing certain heavy metals. Of special interest is the capacity of impregnated fabric to complex mercury, since mercury is one of the more undesirable contaminants in water. It has been visulized that these fibrous materials can well serve to remove many irritants from the air upon being used as filtering devices. Exploratory investigations indicate further value of the fibrous materials prepared by the process of this invention, i.e., rot and mildew resistance can be imparted by the implementation of the process.
The following examples are presented to illustrate some of the preferred embodiments of this invention and should not be construed as limiting the invention in any manner whatever.
EXAMPLE 1 Eight different samples for the formation of the prepolymer are shown in the following table (Table l). The proportion of halide to ethylenimine may be varied as desired but the most useful and easily controlled molar proportion is that set forth in Sample 5. The temperature' in all cases must be controlled within the range of about to 50C in order to prevent the reaction from becoming violent. When the prepolymer is formed (in about 16 hours when the temperature is kept at about C) it is ready for use in preparing padding solutions. When the prepolymer is dissolved in a solvent such as alcohol or water to form about 5% to percent solution, it is tabled for several days but when applied to fabric at a wet pickup of about from 50 percent to 150 percent and the solvent is allowed to evaporate a polymer network is formed within the cotton or other fibrous structure to which it is applied.
both volatile components. for about 16 hours at a temperature of 25C. The partial polymerization which occurred during this time manifested itself by a gradual increase in viscosity of the mixture. The mixture at this point is referred to as a prepolymer. The prepolymer was poured into a shallow dish and allowed to cure upon standing another 16 hours but this time in an open vessel, since no significant vaporaization was observed. The shallow dish had been previously coated with silicone grease to insure non-adhesion. At the end of the second 16 hours period a clear. solid polymer was formed and behaved in the manner referred to as cheesy.
EXAMPLE 3 PREPARATION OF THE POLYMER (using Tris(2- chloroethyl)phosphoramide):
To illustrate the preparation of the prepolymer, employing tris (2-chloroethyl)phosphoramide as initiator and crosslinking agent, a mixture 20 parts by weight of tris(2-chloroethyl)phosphoramide and 80 parts by weight of ethylenimine was prepared and set aside. and handled in the same manner as that of Example 2. obtaining substantially the same results.
EXAMPLE 4 IMPREGNATION OF COTTON SUBSTRATE (to produce in situ formed ethylenimine network polymer.
TABLE I PREPOLYMER FORMULATIONS' HALIDE f ETHYLENlMlNE Sample Compound Formula wt moles wt moles 'l l,2-dlchloroethane CICH OH CI 5 0.05 95 2.20
2 1,2-dlchloroethane CICH OH Cl 25 0.25 L75 3 Tris -chloroethyl)phosphoramide 0=P- (NHCH CH CU 20 0.70 l .86 4 Bls (gzcehloroethylvlnyl )phosphon- CH CH (OCH CH CU 5 J 75 l .70 Trls(2,3-dlbromopropyl)phosphate 0=F-(0CH CH CH Br) 20 3 9 0 6 Trls(l ,3-dichloroisopropyl)phosphate O=P- (0CH CH CH CU 2o 0.0 i 80 I .86
7 B,B'-dichl0r0ethyl ether CICH OH OCH CH CI 2O 0."! 80 1.86
8 Dlchloromethane CH CI H) 0.12 2.00
Time for prepolymer to be formed: 2 to 16 hours Temp: 25c
Prof-0H, H
r, etc.
1/ Thls table only shows the halides that were tested as inltiaters for prepolymer preparation and crosslinking of ethylenimine.
EXAMPLE 2 PREPARATION OF THE PREPOLYMER (using 1,2-dichloroethane): A mixture 25 parts by weight of initiator and crosslinking agent 1,2-dichloroethane and 75 parts by weight ethylenimine was prepared and set aside in a stoppered flask to prevent evaporation of employing ethanol solvent):
A swatch of cotton printcloth weighing 17.8 grams was treated with a 5 percent w/w solution of the propo- 5 lymer of Example 2 in ethanol, to a wet pickup of percent. The wet impregnated fabric was hung on a line and left unmolested at room temperature 25C) for 16 hours. It was then washed in flowing tap water for about 30 minutes and again hung to dry for another 16 hours at room temperature. When the fabric was removed from the drying line it was dry and it was evaluated for weight gain and nitrogen content. The weight gain (add-on) was 5 percent and the nitrogen content was 1.6 percent.
EXAMPLE 5 lMPREGNATlON OF COTTOM SUBSTRATE (to produce in situ formedethylenimine network polymer, employing water solvent):
Repeating the processing of Example 4 and employing the same quantities and values therein, it was observed that the results were identical, when water was used as a solvent.
EXAMPLE 6 IMPREGNATION OF COTTON SUBSTRATE (to produce in sity formed ethylenimine network polymer employing a tris(2-chloroethyl)phosphoramide with ethanol as solvent): A swatch of cotton printcloth weight 17.6 grams was treated with a percent w/w ethanolic solution of prepolymer which was prepared as described in Example 3. The wet pickup was 115 percent. The wet impregnated fabric was hung on a line and left unmolested at room temperature (C) for 16 hours. It was the washed in flowing distilled water for about minutes and again hung to dry for another 16 hours at room temperature. When the fabric was removed from the drying line it was dry. It was then evaluated for weight gain, nitrogen and phosphorus content, and overall appearance. The weight gain (add-on) was 15.8 percent. The nitrogen content was 3.62 percent and the phosphorous content was 0.32 percent.
EXAMPLE 7 EXAMPLE 8 USE OF POLYMER AS SCAVENGER Mercury forms a complex with the network polymer which was formed in situ in the structure of cotton fabric.
The network polymer formed in situ by the process of Example 4 was soaked for 1 hour in a 2.0 percent w/w solution of mercuric chloride. The fabric was then removed from the solution and washed with flowing distilled water. The washed fabric was allowed to air dry at room temperature and chemically analyzed. The mercury content was 3.45 percent.
EXAMPLE 9 USE OF POLYMER AS SCAVENGER Mercury complexed with a network polymer which was formed The process of Example 8 was employed with the fabric of Example 6. The finished fabric contained 3.71 percent mercury.
EXAMPLE 10 USE OF POROUS PAPER AS A SUBSTRATE A porous paper towel was processed in the same manner and using the same chemical mixture of Example 2. The add-on was 48 percent, after washing, and the nitrogen content was 7.29 percent.
EXAMPLE 11 USE OF PEANUT SHELLS AS SUBSTRATE A quantity of peanut shells was ground to pass a 20 mesh screen and 26 grams were impregnated by soaking in a 20 percent solution of the prepolymer of Example 2. The shells were collected on a sintered glass filter and air was pulled through until the wet pickup was percent. The wet impregnated peanut shells were then allowed to dry in an open dish for 16 hours at 25C and suspended in water, then collected on a filter and washed with distilled water 10 times. The shells were then allowed to air dry and then evaluated. The add-on was 38 percent and the nitrogen content was 5.25 percent.
We claim:
1. A method for producing in situ formed, crosslinked polyethylenimine in a fibrous material, the method comprising:
a. mixing ethylenimine with an alkyl halide selected from the group consisting of 1,2-dichloroethane. tris( 2-chloroethyl)phosphoramide, bis( 2-chloroethylinyl )-phosphonate, tris( 2.3- dibromopropyl)phosphate, tris( 1,3- dichloroisopropyl)phosphate, B,B'-dichloroethyl ether and dichloromethane in a molar ratio of about from 44:1 to 27:1;
b. allowing the mixture to stand at 10 to 50 C for from 2 to 16 hours, thereby forming a prepolymer;
c. diluting the mixture in water or ethanol to obtain a 5 to 50 percent concentration of the prepolymer;
d. impregnating the fibrous material with the prepolymer of step (c) to obtain a wet pickup of about from 50 to percent; and
e. allowing the impregnated material to dry at about 25 C until the prepolymer is crosslinked and polymerized.
2. The method of claim 1 wherein the fibrous mate rial is celluslosic.
3. The method of claim 1 wherein the alkyl halide is selected from the group consisting of bis(2- chloroethylvinyl)phosphonate, tris (2,3- dibromopropyl)-phosphate and tris( 1,3- dichloroisopropyl)phosphate.
4. The method of claim 1 wherein the alkyl halide is selected from the group consisting of 1,2- dichloroethane, dichloromethane and B,B- dichloroethyl ether.
5. The method of claim 1 wherein the alkyl halide is tris( 2-chloroethyl)phosphoramide.
Claims (5)
1. A METHOD FOR PRODUCING IN SITU FORMED CROSSLINKED POLYETHYLAMINE IN A FIBROUS MATERIAL, THE METHOD COMPRISING A. MIXING ETHYLENIMINE WITH AN ALKYL HALIDE SELECTED FROM THE GROUP CONSISTING OF 1,2-DICHLOROETHANE, TRIS(2CHLOROETHYL)PHOSPHORAMIDE, BIS(2-CHLOROETHYLINYL)PHOSPHONATE, TRIS(2,3-DIBROMOPROPYL)PHOSPHATE TRIS(1,3-DICHLOROSPHORAMIDE)PHOSPHATE, B,B''-DICHLOROETHYL ETHER AND DICHLOROMETHANE IN A MOLAR RATIO OF ABOUT FROM 44:1 TO 27:1; B. ALLOWING THE MIXTURE TO STAND AT 10* TO 50*C FOR FROM 2 TO 16 HOURS, THEREBY FORMING A PREPOLYMER C. DILUTING THE MIXTURE IN WATER OR ETHANOL TO OBTAIN A 5 TO 50 PERCENT ONCENTRATION OF THE PREPOLYMER; D. IMPREGNATING THE FIBROUS MATERIAL WITH THE PREPOLYMER OF STEP (C9 TO OBTAIN A WET PICKUP OF ABOUT FROM 50 TO 150 PERCENT )T; AND E. ALLOWING THE IMPREGNATED MATERIAL TO DRY AT ABOUT 25*C UNTIL THE PREPOLYMER IS CROSSLINKED AND POLYMERIZED.
2. The method of claim 1 wherein the fibrous material is celluslosic.
3. The method of claim 1 wherein the alkyl halide is selected from the group consisting of bis(2-chloroethylvinyl)phosphonate, tris (2,3-dibromopropyl)-phosphate and tris(1,3-dichloroisopropyl)phosphate.
4. The method of claim 1 wherein the alkyl halide is selected from the group consisting of 1,2-dichloroethane, dichloromethane and B,B''-dichloroethyl ether.
5. The method of claim 1 wherein the alkyl halide is tris(2-chloroethyl)phosphoramide.
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US279919A US3885069A (en) | 1972-08-11 | 1972-08-11 | Preparation of crosslinked polyethylenimine and impregnation of cellulosic material with in situ crosslink-polymerized ethylenimine |
US05/545,277 US3976604A (en) | 1972-08-11 | 1975-01-30 | Preparation of ethylenimine prepolymer |
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Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4032452A (en) * | 1975-11-13 | 1977-06-28 | Sybron Corporation | Electrically regenerated ion exchange system |
FR2418203A1 (en) * | 1978-02-24 | 1979-09-21 | Ciba Geigy Ag | PROCESS FOR REMOVING IONS FROM HEAVY METALS FROM AQUEOUS SOLUTIONS |
US4252645A (en) * | 1978-01-26 | 1981-02-24 | Snamprogetti S.P.A. | Biocompatible cellulose triacetate fibres for the purification of blood |
US4277345A (en) * | 1977-03-17 | 1981-07-07 | Kernforschungsanlage Julich Gesellschaft Mit Beschrankter Haftung | Method for the recovery of uranium dissolved in sea water |
EP0054778A2 (en) * | 1980-12-20 | 1982-06-30 | S.E. Prof. Jörgensen | Process for preparing an anion exchanger, and its use |
EP0117478A1 (en) * | 1983-02-14 | 1984-09-05 | Cuno Incorporated | Modified polysaccharide supports |
US4663163A (en) * | 1983-02-14 | 1987-05-05 | Hou Kenneth C | Modified polysaccharide supports |
US4804686A (en) * | 1986-05-13 | 1989-02-14 | Purdue Research Foundation | Cation-exchange support materials and method |
WO1991019675A1 (en) * | 1990-06-20 | 1991-12-26 | Ricoh Kyosan, Inc. | Method and device for purifying water |
WO1996028605A1 (en) * | 1995-03-13 | 1996-09-19 | Basf Aktiengesellschaft | Use of aminomethylene phosphono group-containing polymers as complexing agents |
WO1997040088A1 (en) * | 1996-04-23 | 1997-10-30 | Basf Aktiengesellschaft | Process for producing finely divided, water-insoluble aziridine polymers |
WO1998002482A1 (en) * | 1996-07-11 | 1998-01-22 | Basf Aktiengesellschaft | Methof of manufacturing finely divided, water-insoluble polymers of aziridines, as well as modified, water-insoluble polymers of aziridines, and their use |
US20020160271A1 (en) * | 2000-12-29 | 2002-10-31 | The Board Of Reagents Of The University Of Oklahoma | Conductive polyamine-based electrolyte |
WO2002101140A1 (en) * | 2001-06-11 | 2002-12-19 | Nano-Tex, Llc | Modification of fabric fibers |
WO2003011453A1 (en) * | 2001-07-26 | 2003-02-13 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Adsorber materials made of renewable raw materials, method for the production thereof and their use |
US20040166753A1 (en) * | 2002-06-10 | 2004-08-26 | Millward Dan B. | Modification of fabric fibers |
US20060162090A1 (en) * | 2002-11-05 | 2006-07-27 | Offord David A | Odor-absorbing cellulosic fibrous substrates |
US20090092572A1 (en) * | 2007-10-01 | 2009-04-09 | Nano-Tex, Inc. | Modification of cellulosic substrates to control body odor |
US20160039985A1 (en) * | 2013-03-28 | 2016-02-11 | Siemens Aktiengesellschaft | Cellulose material having impregnation and use of the cellulose material |
WO2017030609A1 (en) * | 2015-08-17 | 2017-02-23 | Extractmetal, Inc. | Shredded ion exchange paper |
DE102017007273A1 (en) * | 2017-08-01 | 2019-02-07 | Instraction Gmbh | Removal of bacteria from drinking water via filtration |
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US2972606A (en) * | 1956-05-31 | 1961-02-21 | Wyandotte Chemicals Corp | Catalytic aminoethylation of cellulose, cellulose derivatives or polyvinyl alcohol |
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Cited By (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4032452A (en) * | 1975-11-13 | 1977-06-28 | Sybron Corporation | Electrically regenerated ion exchange system |
US4277345A (en) * | 1977-03-17 | 1981-07-07 | Kernforschungsanlage Julich Gesellschaft Mit Beschrankter Haftung | Method for the recovery of uranium dissolved in sea water |
US4252645A (en) * | 1978-01-26 | 1981-02-24 | Snamprogetti S.P.A. | Biocompatible cellulose triacetate fibres for the purification of blood |
FR2418203A1 (en) * | 1978-02-24 | 1979-09-21 | Ciba Geigy Ag | PROCESS FOR REMOVING IONS FROM HEAVY METALS FROM AQUEOUS SOLUTIONS |
EP0054778A2 (en) * | 1980-12-20 | 1982-06-30 | S.E. Prof. Jörgensen | Process for preparing an anion exchanger, and its use |
EP0054778A3 (en) * | 1980-12-20 | 1982-08-25 | S.E. Prof. Jorgensen | Process for preparing an anion exchanger, and its use |
EP0117478A1 (en) * | 1983-02-14 | 1984-09-05 | Cuno Incorporated | Modified polysaccharide supports |
US4663163A (en) * | 1983-02-14 | 1987-05-05 | Hou Kenneth C | Modified polysaccharide supports |
US4804686A (en) * | 1986-05-13 | 1989-02-14 | Purdue Research Foundation | Cation-exchange support materials and method |
WO1991019675A1 (en) * | 1990-06-20 | 1991-12-26 | Ricoh Kyosan, Inc. | Method and device for purifying water |
WO1996028605A1 (en) * | 1995-03-13 | 1996-09-19 | Basf Aktiengesellschaft | Use of aminomethylene phosphono group-containing polymers as complexing agents |
WO1997040088A1 (en) * | 1996-04-23 | 1997-10-30 | Basf Aktiengesellschaft | Process for producing finely divided, water-insoluble aziridine polymers |
US6063286A (en) * | 1996-04-23 | 2000-05-16 | Basf Aktiengesellschaft | Modified, fine-particle, water-insoluble aziridine polymer and use therefore for removing heavy metals from aqueous solution |
WO1998002482A1 (en) * | 1996-07-11 | 1998-01-22 | Basf Aktiengesellschaft | Methof of manufacturing finely divided, water-insoluble polymers of aziridines, as well as modified, water-insoluble polymers of aziridines, and their use |
US20020160271A1 (en) * | 2000-12-29 | 2002-10-31 | The Board Of Reagents Of The University Of Oklahoma | Conductive polyamine-based electrolyte |
US7238451B2 (en) * | 2000-12-29 | 2007-07-03 | The Board Of Regents Of The University Of Oklahoma | Conductive polyamine-based electrolyte |
WO2002101140A1 (en) * | 2001-06-11 | 2002-12-19 | Nano-Tex, Llc | Modification of fabric fibers |
WO2003011453A1 (en) * | 2001-07-26 | 2003-02-13 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Adsorber materials made of renewable raw materials, method for the production thereof and their use |
US20040166753A1 (en) * | 2002-06-10 | 2004-08-26 | Millward Dan B. | Modification of fabric fibers |
US20060162090A1 (en) * | 2002-11-05 | 2006-07-27 | Offord David A | Odor-absorbing cellulosic fibrous substrates |
US20090092572A1 (en) * | 2007-10-01 | 2009-04-09 | Nano-Tex, Inc. | Modification of cellulosic substrates to control body odor |
US8778321B2 (en) | 2007-10-01 | 2014-07-15 | Nanotex Llc | Modification of cellulosic substrates to control body odor |
US20160039985A1 (en) * | 2013-03-28 | 2016-02-11 | Siemens Aktiengesellschaft | Cellulose material having impregnation and use of the cellulose material |
US9718934B2 (en) * | 2013-03-28 | 2017-08-01 | Siemens Aktiengesellschaft | Cellulose material having impregnation and use of the cellulose material |
WO2017030609A1 (en) * | 2015-08-17 | 2017-02-23 | Extractmetal, Inc. | Shredded ion exchange paper |
DE102017007273A1 (en) * | 2017-08-01 | 2019-02-07 | Instraction Gmbh | Removal of bacteria from drinking water via filtration |
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