前苏联专利SU1286108A3 Method for producing perfluorinated ion-exchange polymer-base liquid composition

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专利摘要:
A process is provided for making a liquid composition of a perfluorinated polymer having sulfonic acid or sulfonate groups in a liquid medium by contacting the polymer with a mixture of 20 to 100% by weight of water and 0 to 80% by weight of a second liquid component such as a lower alcohol. e.g. propanol or methanol, at a temperature of at least 180°C (at least 240°C when 90% to 100% water is used). in a closed system. The liquid composition made by this process, or modified liquid products prepared therefrom, can be used in coating various substrates, in casting films, and in repairing perfluorinated ion exchange films and membranes. The process is also useful in recovering perfluorinated polymer having sulfonic acid or sulfonate groups from scrap and used articles made of such polymer or contacting such polymer as a component part thereof.
公开号:SU1286108A3
申请号:SU823426505
申请日:1982-04-30
公开日:1987-01-23
发明作者:Густав Грот Вальтер
申请人:Е.И.Дюпон Де Немур Энд Компани (Фирма)；
IPC主号:

专利说明:

Oil
The invention relates to the production of perfluorinated ion exchange materials and can be used in the technology of manufacturing and repairing ion exchange membranes used in electrolysis processes.
The purpose of the invention is to improve the physicochemical properties of products from a liquid composition based on perfluorinated ion-exchange polymers,.
Equivalent masses (EW), which are indicated in the examples, are determined by titration of the polymer in the free acid form with a standard aqueous solution of sodium hydroxide. Such a determination is made with an accuracy of only about ± 25 equivalent mass units.
In the proposed method, a polytetrafluoroethylene (PTFE) copolymer of tetrafluoroethylene and methyl perfluoro (4,7-dioxa-5-methyl-8 nonanoate) is used. (TFE / EVE), tetrafluoroethylene copolymer and perfluoro (3,6-diox-4-methyl-7-octenesulfonyl fluoride) (TFE / PSEPVE),
Example 1 30 ml of n-propanol, 200 ml of water and 40 g of tetrafluoroethylene copolymer and perfluoro (3J6-dioxa-4-methyl-7-octenesulfonyl fluoride) (TFE / PSEPVE) were introduced into a shake flask. with an equivalent mass of 1,100, whose functional groups are hydrolyzed to form — with the polymer itself in powder form. This float bottle is sealed, heated at 240 ° C for 18 hours while shaking simultaneously and cooled. 481 ml of a clear liquid composition having a density of 0.93 g / ml and a viscosity of 12.5 cSt are obtained. The solid polymer in the sediment. not formed A study by X-ray diffraction reveals the presence of colloidal particles about 5-10 microns in size (50A),
As a result, the form of vania by casting portions of this liquid composition and heating at 60-90 ° C, films of average strength are obtained.
Example 2. 200 ml of n-propanol, 500 ml of water and 30 g of TFE / PSEPVE with an equivalent weight of 1100, the functional groups of which are hydrolyzed to form S02Na, are introduced into a shake flask, this polymer
five
is in powder form. The flask is sealed, heated under reflux for 3 hours with one shaking and then cooled. 430 ml of a high-density lower phase is obtained, which is a liquid composition containing a small amount of undissolved gel, and 37 ml of a low-density upper phase, which is mainly dipropyl ethers, which is removed. About 10 ml of the liquid medium are distilled off from 100 ml of the obtained liquid composition. Analysis of the distillate by gas chromatography using an infrared spectrum shows the presence of about 40 wt.% N-propanol, 25 wt.% Isopropanol and 35 wt.% Water,
Example 3. 550 ml of n-propanol, 400 ml of methanol, 1000 ml of water and 200 g of TFE / PSEPVE having an equivalent weight of 1100, the functional groups of which are hydrolyzed to form -, are introduced into a shake flask, the polymer having a powder form. The flask is sealed, heated at 220 ° C. for 3 hours while shaking and cooled. 1441 ml of high density bottom phase is obtained, which is a composition having a density of 1.018 g / ml and a viscosity of 111 cSt, and 62 ml of a low density top phase, which is removed. The solid polymer does not remain in the sediment. To the resulting liquid composition, add tristilfosfat in the amount of; % By weight of polymer content in the resulting liquid product. A film obtained by injection molding a portion of a specified liquid product and gradually heating from 90 to 20 ° C has a yield strength.
0
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0
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8.32x10 ° Pa, tensile strength 1577x10 Pa and ultimate elongation at break of 292%,
Example 4 To a portion of the liquid product obtained according to Example 2, 2-ethoxyethanol is added — a quantity of 50% by volume of the modified liquid product obtained. Catalyst catalyst granules are introduced into the flask in a vortex of porous alumina (Norton SA 5205), then this flask is evacuated to 318
exact pressure of about 20 (M1 Pa (15 mm Hg) and a sufficient amount of this modified liquid product is introduced into it so that the alumina granules are completely covered. The vacuum is released, the liquid product enters the pores of the granules, Respiration to a residual pressure Neither 2000 Pa and discharge of vacuum to atmospheric pressure is repeated three more times. Excess liquid product
removed, and the coated granules are dried at 50 ° C. One of the dried-up coated granules is broken into pieces and a microscope is examined on the inside of the early part of this granule. The study shows a uniform coating of the inner surfaces of the granules.
Example 5 Samples consisting of several sheets are passed through a modified liquid product prepared according to Example 4 and gradually heated to 50-75. The sheets used for the samples are polytetrafluoro fabric 25 of an agglomerated polymer layer
TFE / EVE
shake and cool. Two liquid and one solid phases are removed from the shake flask. The solid phase, which is recovered by passing the entire product through a funnel with a porous glass plate, is an undissolved TFE / EVE copolymer and a reinforcing fabric. A more solid lower liquid phase (368 ml) is a liquid composition corresponding to the proposed method, with a density of 0.94 g with a content of about 6 g of TFE / PSEPVE copolymer per 100 g of liquid comp. The lighter upper liquid solution (172 ml) is removed. The solid phase remaining on the filter is washed with bright methanol. As a result, 29 g of conglomerate are obtained, consisting of
ethylene fibers, a 50:50 blend fabric of poly-para-phenylene terephthalamide staple fibers and polymetaphenylene isoftalamide staple fibers, a 30 fiber glass fabric, an asbestos fiber sheet and a microporous PTFE sheet having microstructure in the form of nodules interconnected by fibrils (material produced by W, L Gore and Associates, Zne under the trade name Gore-Te x),
Example 6 A defective cation-exchange membrane comprising a layer of TFE / PSEPVE 40, hydrolyzed to a SO — Na form, having a small diameter orifice, is repaired by applying a drop onto the said aperture. 45 th liquid product, prepared as described in Example 4, and gradual
heating from 50 to 75 C,
Example 7: 300 ml of n-propanol, 50 50 ml of methanol, 350 ml of water and 50 g of scraped membrane having one layer of TFE / PSEPVE in the form with an equivalent weight of 1.100, one layer of a copolymer of tetrafluoroethylene and Methyl- 55 perfluoro (4,7-diox-5-methyl-8-nonanoate (TFE / EVE) in the form of COOCHjC with an equivalent weight of 1050 and a reinforcing fabric made of polytetrafluoroethylene and polytetrafluoroethylene fibers. Part of this agglomerated TFE / EVE polymer is separated polytetrafluoroethylene fibers are formed to form a transparent, heavy film. Analysis using The infrared spectrum did not detect the presence of a sulfonate component in this film.
Example 8, Shock is made from pieces of tightly bound polytetrafluoroethylene fabric using strips of tetrafluoroethyl / hexafluoropropylene copolymer, which is hermetically sealed with a roar of the holes in the broom. Before the final hermetic sealing of the bag versions, 50.66 of the TFE / PSEPVE copolymer hydrolyzed to the VOZH form, with an equivalent mass of 1100 in the form of a powder, 10–35 mesh in size (O, 5-2, mm ) The hermetically sealed bag containing the sulfonic acid copolymer is placed in a vacuum drying oven, in which it is first kept at 60 ° C for 5 hours, and then at a constant temperature for 2 days, moisture is lost (2.50). d). This suggests that the mass amount of the copolymer of dried sulfonic acid is 48, 16
This hermetically sealed mesh with polymer is placed in a shake.
curl, and this membrane is cut into pieces approximately 1.3 x X 1.3 cm in size. The flask injected is sealed, heated at 210 ° C for 18 hours while simultaneously
15
0 5 of agglomerated polymer layer
shake and cool. Two liquid and one solid phases are removed from the shake flask. The solid phase, which is recovered by passing the entire product through a funnel with a porous glass plate, is an undissolved TFE / EVE copolymer and a reinforcing fabric. A more solid lower liquid phase (368 ml) is a liquid composition corresponding to the inventive method, with a density of 0.94 g / ml, with a content of about 6 g of TFE / PSEPVE copolymer per 100 g of liquid composition. The lighter upper liquid phase (172 ml) is removed. The solid phase remaining on the filter is flashed with hot methanol. As a result, 29 g of the conglomerate consisting of
TFE / EVE
and polytetrafluoroethylene fibers. A part of this agglomerated TFE / EVE polymer is separated from polytetrafluoroethylene fibers, molded to form a transparent heavy film. Analysis using the infrared spectrum did not detect the presence of a sulfonate component in this film.
Example 8 A bag is made of pieces of tightly woven polytetrafluoroethylene fabric using strips of tetrafluoroethyl / hexafluoropropylene copolymer, by sealing hermetically by heating the mesh. Before the final hermetic sealing of the bag openings, 50.66 g of TFE / PSEPVE copolymer hydrolyzed to the VOZN form with an equivalent weight of 1100 in the form of a powder with a particle size of 10-35 mesh (0, 5-2, mm) are introduced into it. The bag containing the sulfonic acid copolymer is placed in a vacuum drying oven, in which it is first kept at 60 ° C for 5 hours and then at room temperature for 2 days, while moisture loss (2.50 g) is observed. This suggests that the mass amount of the copolymer of the dried sulfonic acid is 48-, 16 g
This hermetically sealed polymer bag is placed in a shakeable
51
the flask together with 200 ml of water, which is sealed under pressure and heated to 240-255 ° C for 100 hours while stirring, the pressure at 240 ° C is 2.5x10 Pa, and at 255 ° C it is 3.25x10 Pa. Then the vessel is cooled to room temperature at which the pressure in it is I, 7x x 10 Pa (25 psi). When removing the containing vessel, a viscous liquid composition was found, corresponding to the proposed method, containing gelled samples of a sulfonic acid copolymer and a polytetrafluoroethylene bag (which remained undamaged ) with a small amount of polyme and the inside and outside with a polymeric film it polytetrafluoroethylene ethylene bag and its contents were washed with hot water, dried at 50 C and weighed in the bag remains lshi 15.8 g of sulfonic acid copolymer.
The viscous liquid composition is separated from the gelled polymer by passing through a funnel with a porous glass filter plate. Weighing the gelled samples, bag content and film outside the bag after drying n states that in the resulting viscous liquid composition, 4.4 g of a sulfonic acid copolymer remains at room temperature, which is approximately 7.2 g of the indicated copolymer per 100 ml of the liquid composition. Films formed from this liquid composition in water are brittle; however, adding a certain amount of n-propanol to a portion of this liquid composition in water produces strong films.
The sulfonic acid film formed from the outer surface of the bag after drying has high mechanical properties.
The presence of both sulfonic acid copolymer films on the outside of the bag and gelled sulfonic acid copolymer samples in liquid on the outside of the bag shows that at elevated temperatures during the heating step, the concentration of copolymer in the liquid composition becomes even more than 7.2 g of the copolymer 100 ml of the liquid composition, and in addition, a portion of the copolymer is converted to a solid product upon cooling.
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0 0
About 5 0
five
d
086
Example 9: 325 ml of 2-ethoxyethanol, 175 ml of water and 40 g of TFE / PSEPVE with an equivalent weight of 1120, the functional groups of which are hydrolyzed to form-SOjK, are introduced into a shake flask, this polymer is in the form of cubes. The flask is closed, heated to 230 ° C. for 3 hours while shaking, and cooled. The first clear liquid composition is obtained, none of the solid polymer cubes remain in this liquid, but a small amount of film pieces is removed by filtering. As a result of evaporation to dry portions of this filtered liquid composition in an amount of 20 ml, 15668 g of polymer are obtained. This indicates that the concentration of polymer in the liquid composition is 8.34 g of polymer per 100 ml of liquid composition,
250 ml of the first composition containing the copolymer in the 50-50 form was injected into the flask. (A TFE / PSEPVE copolymer tube 3 m long, 0.76 mm in diameter, 0.13 mm thick, with an equivalent weight of 1100 (the copolymer in the form -SOjH) is coiled and inserted into a flask so that both ends of the tube exit the neck of the flask. A solution consisting of 20 ml of concentrated hydrochloric acid, 50 ml of water and 130 ml of 2-ethoxyethanol is prepared. the solution slowly flows into the flask through the inside of the tube under the action of its own force of gravity, while at the same time Samples (20 ml each) flowing out of the liquid tube are collected at intervals, evaporated to dryness and the resulting KC1 is taken up. From the first, second and third samples, respectively, 0.133, .0.043 and 0.029 g KS1 are obtained. , introduced into the flask, is converted into a second liquid composition, in which the l functional groups of the polymer are transformed into - SO H groups by ion exchange.
A portion of the second liquid composition is cast and heated to, resulting in a strong film,
Examples 10-14 (comparative), In each of these examples, 10 g of TFE / PSEPVE copolymer, which
7
hydrolyzed either to form-SOjK (examples 10-12), or to form-SOjH (examples 13-14), having an equivalent weight, indicated in table. 1, in the form of a film with a thickness of 100 µm, is introduced into 100 g of the liquid medium indicated in Table 1, and heated under reflux for 4 hours. After cooling, the amount of 2861088 is determined.
as a result, 543 ml of a high-density phase with a density of 0.989 g / ml and 48 ml of a low-density phase (upper phase K) are poured.
Repeated treatment of the upper phases as a by-product is carried out as follows.
450 ml of water are introduced into the shake flask, the upper phases K, L and M,
in the polymer in the liquid phase, by evaporation of the JO and 40 g of TFE / PSEPVE copolymer with equilibration of 50 ml of the sample to dryness and weighing the residue after evaporation. The results are presented in table 1. In most cases, the amount of the solute is negligible and is at most 0.54% by weight.
Example 15 (comparative), 10 g of copolymer are introduced into 100 ml of water
1200, hydrolyzed to form-50.N, Flasks are sealed, heated to 220 ° C for 3 hours and cooled. 368 ml of a high-density lower phase (density 1.003 g / ml) containing 4.6 g of sediment and an additional 10 ml of low-density upper liquid phase are obtained, which is removed. In this way.
TFE / PSEPVE, hydrolyzed to the formulated recirculation process, is
25
thirty
We have an equivalent weight of 1050 in the form of a film with a thickness of 100 µm, and this mixture is stirred and heated at 68 ° C and the amount of polymer in the liquid phase is determined after evaporation by evaporation to 50% of a portion and weighing the residue after evaporation to dryness for 3 hours. The liquid phase contains only 0.022% by weight of polymer.
Example 16: 180 ml of n-propanol, 150 ml of methanol, 350 ml of water and 40 g of TFE / PSEPVE with an equivalent weight of 1100, which is hydrolyzed to form-SOjH and is in powder form, are introduced into a shake flask. The flask is sealed, heated to 230 ° C for 3 hours while shaking, and cooled. 420 ml of a high-density phase, which is a liquid composition corresponding to the proposed method (density of 0.995 g / ml), and 43 ml of low-density phase (upper phase K) are obtained,
The process is carried out in the same way using 200 ml of n-propanol, 150 ml of methanol, 350 ml of water and 60 g of the same polymer and heating is carried out at 220 ° C for 3 hours, resulting in 548 ml of the dense phase with density of 1, 00 g / ml; viscosity of 51 cp and 82 ml of low-density phase (upper phase L).
35
40
.45
. 861088
as a result, 543 ml of a high-density phase with a density of 0.989 g / ml and 48 ml of a low-density phase (upper phase K) are poured.
Repeated treatment of the upper phases as a by-product is carried out as follows.
450 ml of water are introduced into the shake flask, the upper phases K, L and M,
-JO and 40 g of TFE / PSEPVE copolymer with equivalent -
and 40 g of TFE / PSEPVE copolymer with an equivalent
1200, hydrolyzed to form-50.N, Flasks are sealed, heated to 220 ° C for 3 hours and cooled. 368 ml of a high-density lower phase (density 1.003 g / ml) containing 4.6 g of sediment and an additional 10 ml of low-density upper liquid phase are obtained, which is removed. In this way.
this recycling process is
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ABOUT
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successful because it provides 381 ml of a liquid composition containing about 35 g of polymer.
Example 17. In a shake flask, 300 ml of n-propanol, 50 ml of methanol, 300 ml of water and 30 g of TFE / PSEPVE copolymer having an equivalent of 1200, the functional groups of which are hydrolyzed to form-BO, and the scholimer B is in the form of a poroj with a particle size of 35-60 mesh (0, 50 mm). The flask is sealed, heated to 230 ° C. for 4 hours while shaking, and cooled. 190 ml of low density upper phase are obtained, which is removed, and 380 ml of high density lower phase (density 1.00 g / ml),
No precipitate of the polymer remains. A portion of the high-density phase (80 ml) was boiled to remove some water from it, and at the same time 50 ml of n-propanol was gradually added until a final volume of 35 ml was reached. Then 15 ml of 2-ethoxyethanol are added, resulting in a modified liquid product.
A piece of TFE / PSEPVE film with an equivalent weight of 1100, 125 µm thick (5 mile), into which a reinforcing fabric (tissue in flat
The process is carried out in the same manner. With the interlacing of which as on the base.
at once using 200 ml of n-propanol, 150 ml of methanol, 350 ml of water and 40 g of the same polymer. Heating is carried out at 230 ° C for 3 hours.
and in duck, there are 16 polytems of rafluoroethylene yarns weighing 400 denier per centimeter) / and with functional groups, the basis of which is hydrolyzed.
and in duck there are 16 polytetrafluoroethylene yarns weighing 400 denier per centimeter by weight) / and with functional groups, hydrolyzed 9-12
first, they are dusted with n-propanol, then coated on one side (opposite from the side into which the reinforcing fabric is inserted) with the specified modified liquid product and dried, resulting in a coated membrane.
A piece of coated membrane is placed between the compartments of a small chlor-alkali element, covered with the side facing the cathode space, and the electrolysis of a saturated aqueous solution of sodium chloride is performed at a current density of 2.0 A per 1 inch (ASI) (or 0.3 A / cm ) at 80 ° C. The electrolysis process lasts 18 days, as a result of which 20 wt.% Of caustic soda is obtained at a voltage of 3.5-3.7 V and with a current efficiency of 68%,
Examples 18-39 and comparative 40-42. Water and / or other liquid components, as well as TFE / PSEPVE, are injected into the shake flask, the quantities of all these components being equivalent to the weight of the polymer and its shape is given in Table 2. The tube is closed and heated for a period of time and at a temperature that is indicated in table 2. The results obtained, regardless of whether the polymer is completely dissolved or not, the amount and concentration of the resulting liquid composition and, in some cases, the viscosity, are also listed in Table 2.
The proposed method has the advantage of providing a fast method for producing liquid compositions that were not previously commercially available and which are used in many industries.

权利要求:
Claims (4)
[1]
Invention Formula
I. A method for producing a liquid composition based on a perfluorinated l ion-exchange polymer containing functional groups of the formula
SO, M
where M is H and Na, or K,
by mixing said polymer with
08
ten
solvent, in order to improve the physicochemical properties of products based on the composition, a polymer with an equivalent mass of 105P-1500 is used as the polymer, and water or a mixture is used as the solvent; 20-80% by weight of water; and 20-80% by weight of a compound selected from the group comprising methanol, ethanol, n-propanol, n-butanol, 2-butanol, 2-methoxyethanol, 2-ethoxyethanol, ethylene glycol dimethyl ether , diethylene glycol dimethyl ether, dioxane and acetonitrile, mixing is carried out at 170-250 C in a closed vessel for 3-18 hours, followed by concentration by distillation of the solvent.
[2]
2. Method pop. 1, which differs from the fact that after distilling off the solvent, triethyl phosphate is introduced into the composition in an amount of 100-110% by weight of the polymer.
[3]
3. Method by clause 1, which is different from the fact that after distilling off the solvent, 2-ethoxyethanol is introduced into the composition in an amount of 43-50% of the volume of the liquid composition.
[4]
4. The method according to claim 1, about tl and h and yu and the fact that the liquid composition of a perfluorinated ion-exchange polymer containing grzttpy -SOjM, where M is Na or K, is subjected to treatment with cation exchange resin in acid form,
T a b l and c a I
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0
10 1 1 12
13 14
1050 1050 1050
1050 1300
Ethanol, 95.0.0 Water 100.006
Iopropyl- 0.01 alcohol 100
Isopropyl-0.54 alcohol alcohol 80, water 20
Water 100 0.04
Tsblitsa 2

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法律状态:

优先权:

申请号 | 申请日 | 专利标题

US06/259,506|US4433082A|1981-05-01|1981-05-01|Process for making liquid composition of perfluorinated ion exchange polymer, and product thereof|

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