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    • 专利摘要:
    1475879 Solid adsorbent for gases MINNESOTA MINING & MFG CO 6 June 1974 [25 May 1973] 25181/73 Heading B1L [Also in Division C3] Gases are preferentially sorbed by a thermoset foam which has been prepared by the pyrolysis of a liquid composition comprising at least one aromatic nitrogen-containing compound having the general formula: in which Ar represents an aromatic nucleus on which X and Y are substituents and which optionally carries additional substituents, X represents a substituent having a negative Hammett sigma constant (i.e. having a reducing action) and attached to the aromatic nucleus by a nitrogen, oxygen or sulphur atom, and Y represents a substituent having a positive Hammett sigma constant (i.e. having an oxidising action) and attached to the aromatic nucleus by a nitrogen atom, the substituents X and/or Y optionally forming part of a ring fused onto the aromatic nucleus. In example 8 the foam was used to sorb HCl, SO 2 , HCN, H 2 S, HF and Cl 2 . The foams may be used to remove notions or poisonous gases, e.g. HCN or HF, from air, and H 2 S and SO 2 from combustion waste gases, and may be mixed with activated charcoal for such uses.
    公开号:SU929005A3
    申请号:SU742044312
    申请日:1974-05-24
    公开日:1982-05-15
    发明作者:А.Эрред Люкс；А.Синклер Роберт；Н.Фергюсон Аллан
    申请人:Минесота Майнинг Энд Мануфакчуринг Компани (Фирма)；
    IPC主号:
    专利说明:

    Compounds selected from the group consisting of nitroaniline, 4-nitrophenol, 2-chloro-β-nitroaniline, 2-methyl-4-nitroaniline, 2-amino-nitrophol NOL, 3 methyl-β-nitrophenol are used as aromatic compounds. The resulting thermosetting foam has a specific surface area of at least 50, has very good chemisorbing properties, and is thus a personal sorbent material for polar molecules, for example, organic acids and bases, organic halide compounds, such halotenes as chlorine, bromine and iodine, strong acids, such as HC1, other acids such as HF, and IMS, heavy metal ions, such as. Ld and out. liquids, nitrogen oxides, e.g. N0 and sulfur oxides, e.g. SO and 50 3 Such polar molecules form a chemical bond with the sorbent material and are thus strongly retained compared to the free physical adsorption of activated carbon. In addition, thermosetting foams retain most of their sorption capacity even in the heated state. Thermosetting foam is a good sorbent for most gases and vapors and may have physical adsorbing properties close to those of activated carbon. However, in most cases, activated carbon has better physical adsorption properties for neutral organic molecules, such as hexane, benzene and ethyl acetate, and therefore it is sometimes useful to use a mixture of thermosetting foam and activated carbon to get excellent chemisorption of polar molecules and good physical adsorption of other molecules. The aromatic compound containing nitrogen is pyrolyzed by heating it to a relatively low temperature, e.g. 200-230 ° C, but as soon as pyrolysis starts, an exothermic reaction occurs and it is obvious that the temperature of the whole mass can rise to. However, there may be areas within the mass in which the temperature is much higher. After the start of the exothermic reaction, no additional external heating is required and heating to the pyrolysis temperature is necessary just to start the reaction. As the reaction proceeds, a sudden and large expansion occurs, resulting in the formation of porosity of the thermosetting foam, which may have an apparent volume hundreds of times larger than the original volume. Therefore, until careful precaution is taken to maintain the temperature of pyrolysis or the purification of thermosetting foam, this foam will contain unreacted material and condensed low-molecular-weight low-melting fusible substances that are carcinogenic or toxic. The most effective way to obtain a pure product is to carry out the reaction to the very end, in which foam is formed. This is easier to do by maintaining the foam at the reaction temperature after the KOI and the heat generated by the exothermic reaction become insufficient to maintain such an elevated temperature. Thus, it is necessary to monitor the reaction temperature and as soon as the temperature begins to fall, add sufficient heat to maintain this temperature for an additional 20 minutes to 3 hours. If the foamy product has cooled after formation, it can be heated again in an inert atmosphere to obtain the same result. This method also leads to an increase in the specific surface of the foam. Foam material can be extracted to remove harmful materials. For example, the foam can be pulverized and washed with an acid, such as dilute HC1, or a base, such as dilute NaOH, and an organic solvent, such as acetone. Between each wash, the powder can be regenerated by filtration and washed with water. This helps to remove all traces of raw materials and substances with low molecular weight. This method of producing foam can also be carried out at high pressure (superbarometric pressure up to 150 atm or more), which keeps the product in a compressed state (without a significant reduction in the potential of the high specific surface area of the foam). Compression leads to the complete heating of the products and the completion of the reaction. Thermosetting foam is non-carcinogenic and non-toxic, has no low-molecular-weight meltable toxic components, and is safe for humans. Fusible materials referred to in the invention are partially melted starting materials with a low molecular weight. This thermosetting foam contains nothing except traces of starting material or fusible substances with low molecular mass.
    by cooler weight, e.g. no more than 0.0011 by weight of any of them, and even residual traces like these are occluded inside the foam and therefore contact with them ceases when dealing with foam.
    To ensure that thermosetting foam is non-carcinogenic and non-toxic, it can be obtained in its pure state if all of the pyrolysis of OS-25 exists when such material is introduced into the reaction zone that, despite a sudden and strong increase in apparent volume, the entire reaction material maintained at pyrolysis temperature after formation, or by thorough purification, for example, washing with dilute acids, water, dilute bases, aqueous and organic solvents. The advantage of washing with an organic solvent is that it participates in expelling water from the foam, and in the case of volatiles it can be removed by evaporation. If necessary, thermosetting foam can be thoroughly cleaned and reheated, at least up to the pyrolysis temperature. Black thermosetting foams are obtained by pyrolysis of the liquid composition, i.e. liquids at the pyrolysis temperature, to obtain a solid foam, and not during carbonization of the carbonaceous solid material, to obtain solid charcoal. Thus, the porous structure of the foams is formed during the pyrolysis process and is no longer present in the pyrolyzed material. In fact, the condensation reaction occurs during the process of pyrolysis by catalysts of which the acid and the strong base can be strong. Therefore, an aromatic compound, co9
    nitrogen. Thus, an aromatic compound, containing nitrogen, which is liquid at the pyrolysis temperature, can be subjected to pyrolysis, either in pure form or in a mixture with other components, which forms from liquid components. In order to carry out efficient pyrolysis, the volatility of the components at a temperature of 30-5 holding nitrogen should have a structure that easily condenses, and the liquid mixture that undergoes pyrolysis, in addition to aromatic nitrogen containing compounds, should include one or more compounds that are promoters of condensation of an aromatic compound containing nitrogen, for example, because they are dehydrating reagents for the aromatic compound containing nitrogen and / or co-condensed with it. There are ways to carry out the pyrolysis of liquid formulations, including an aromatic compound containing pyrolysis should not be too high. If the components are gaseous at the pyrolysis temperature, they will evaporate from the liquid composition. These components, as mentioned above, serve as promoters for the condensation of an aromatic compound containing nitrogen. One group of compounds that serve as promoters of this condensation is dehydrating reagents for an aromatic compound containing nitrogen, for example, strong mineral or organic acids and strong bases, and the other is compounds that are cocondensed with the aromatic compound containing nitrogen, and TC in the form of cross-links in the structure of the foam. This is believed to lead to the establishment of the desired porous structure of thermosetting foams at an early stage of the pyrolysis of an aromatic compound containing nitrogen. The latter group includes organic acids. Examples of suitable strong acids are mineral acids, such as true and phosphoric or or-. Hydroxy acids, such as methanesulphonic acid or fluorinated methanesulphonic acids, and examples of strong bases are mineral bases, such as caustic soda or caustic potassium. Latent acids can also be used, i.e. compounds which
    easily decomposed when heated to the pyrolysis temperature and form strong acids. Examples are the amine salts of strong acids, for example .. (CH3) 3NS03 and CH3H3WH3. An aromatic compound containing nitrogen can also be pyrolyzed in a mixture with an organic acid lot, such as oxalic acid or adipic acid, which can condense with the aromatic center containing nitrogen and, in some cases, to give foams with an increased specific surface. However, when used, it is desirable to include a strong acid in the liquid mixture undergoing pyrolysis. The aromatic compound containing nitrogen can also be pyrolyzed in a mixture with a soluble salt, preferably in the presence of an additional amount of a strong acid or base. Examples of suitable soluble salts are sodium sulfate, sodium chloride, sodium bisulfate, and primary sodium phosphate. These soluble salts are believed to act like layers formed by filler, or pores between condensable reacting molecules during pyrolysis, thereby contributing to the determination of the required molecular structures. After removal of these salts, for example by leaching, a porous structure is retained. The resulting surface area depends on the specific aromatic compound containing nitrogen or a mixture of this compound and other selected components, but the specific surface area may increase with further pyrolysis, for example, with ZOO-BOO C thermosetting foam under controlled atmosphere (nitrogen) conditions which can be saturated with steam. In the process of further pyrolysis, weight loss occurs and increases with specific surface area. The larger the surface area, the greater the amount of material that can be sorbed. Pure non-carcinogenic and non-toxic thermosetting foam preferably has a specific surface area of 50 m / g, it is desirable that the specific surface of the foams be at least 200 and can be equal to 900 Mvr, and when using
    Preferred materials may be even greater.
    Big and sudden increase. Volume reduction during pyrolysis with the formation of a thermoset foam occurs as a result of the release of water vapor and other volatile materials during the reaction.  The resulting material is compared to porosity with large voids.  They do not contribute to the change in specific surface area, which is a measure of the microporous structure of the foam.  The thermosetting foams are believed to have the structure of polychinoxaline, and thus it is obvious that they have a repeating structure with a cross-link between the chains of these repeated condensed aromatic cores, with the positions of the cross-links coming from the carbon atoms to which they are attached. hydrogen atoms after removal of the latter.  Such a structure makes thermoset foam very resistant to heat and oxidation.  For example, part of the foam can be kept in the flame and, although it will accumulate and gradually burn, the burning will immediately stop after it is removed from the flame and it will not decompose as a result of this treatment.  This structure corresponds to the black color of the foam and elemental analysis of the foam with a nitrogen content of 12-20.  With this foam structure, it is obvious that nitrogen atoms impart chemisorption properties.  The higher the percentage of nitrogen in the foam, the better its chemisorption properties.  In addition, depending on the method of its preparation, the foam may contain several functional groups.  If pyrolysis is carried out in the presence of sulfuric or phosphoric acid, then there may be several sulphonate or phosphate groups instead of several hydrogen atoms.  Some functional groups tend to be removed as a result of additional pyrolysis.  Although one or more aromatic compounds containing nitrogen can be pyrolyzed in its pure form, it is preferable to pyrolize a mixture of one or more aromatic compounds containing nitrogen and acids (sulfuric or phosphoric), or a mixture of an organic acid, such as common acid with a mineral acid or a mixture of strong acid and excess salt, such as sodium sulfate, or a strong base, such as caustic soda or caustic potash.  Such a mixture is usually a viscous liquid at room temperature, and since it is slowly brought to the pyrolysis temperature, usually in the range of 200-230 ° C, a homogeneous solution is formed.  Then, a sudden reaction occurs with abundant gas emission, which is mainly water vapor, and black pores with a large volume are formed.  In this production method, thermosetting foam is often formed, which has a relatively small specific surface area, for example, if pyrolysis is carried out in the presence of sulfuric acid, BUT with additional pyrolysis, as indicated above, an increased specific surface area can be obtained.  If pyrolysis is carried out in the presence of phosphoric acid, the foam can have a sufficiently large specific surface area, provided that the molar ratio of acid to aromatic compound is in the range of 1 ,.  If this ratio is less than 1.7, they can form pores with a large volume during pyrolysis with a small specific surface.  After a large volume pore has been formed, it can be crushed and a thermosetting foam powder is obtained.  As a result, large voids in the pores are destroyed, but the specific surface is maintained, which is caused by the microporous foam structure.  The foam powder can then be used or processed (e.g., additional pyrolysis and / or exhaustive extraction) to clean it of carcinogenic materials or other toxic components, or simply to increase its specific surface area.  To clean a thermosetting foam, it can be powdered and the powder washed with acid. for example, dilute HC1, or base, for example, dilute NaOH and organo05.  1st solvent such as acetone.  Between each wash, the powder can be regenerated by filtration and washed with water.  In this way, all traces of the starting materials and low melting substances with low molecular weight can be removed.  The powder of thermosetting foam can be subjected to additional pyrolysis at higher temperatures, e.g., 00 ° C, and under inert atmosphere conditions, e.g., nitrogen atmosphere.  It also leads to an increase in the specific surface of the foam.  After obtaining the powder and its purification or pyrolysis, it can be granulated to give it a form suitable for processing and use as a sorbent. Powder can also be converted. form in an easily processable form, for example, by mixing it with a binder such as cella. a vine or peat, or incorporating it into a fabric, e.g. a felt-like fabric of cellulose.  Thermosetting foam can adsorb very strongly relatively large amounts of polar molecules.  If it is desirable to remove polar molecules from the liquid in which they are contained, the thermosetting foam is introduced into the liquid.  In the event that the liquid is a gas, the gas can be passed over or through a layer of thermosetting foam, which can be in the form of powder, grains or incorporated into the fabric, and in the case of liquid, the foam in the appropriate physical form can be exposed to contact with the liquid.  Thermosetting foams are widely used to remove harmful or poisonous gases from the air.  Thus, they are suitable as active sorbing materials in gas masks or filters for airflow of chemical processes or cooking (cooking), or air conditioners (in pure form or in combination with other known sorbent materials).  For example, if thermosetting foam is used in gas masks, then it is highly effective in removing remote gases, such as HCN or F, which can be in electrochemical metallization processes, HnS and O ;, can be found in the waste of combustion processes, and thermosetting foams in They are very suitable for removing these sulfur compounds and preventing their release to the atmosphere.  Thermosetting foams can also be used in pot lids to absorb unpleasant smells from the kitchen.  In any such use, thermosetting foam can be mixed with activated carbon, which has a high sorption capacity for molecules for which this foam has a relatively low sorption capacity.  Thermosetting foams can also be used to remove undesirable molecules, in particular polar molecules, such as heavy metal ions from liquids, such as water. For example, thermosetting foams are used when drying hydrocarbons moistened with water, such as oil or chlorine-containing hydrocarbons, for example trichlorethylene, which is used in dry cleaning.  Foams can also be used to remove other unwanted molecules from dl liquids. dry clean to clean these liquids for reuse.  In addition, these foams can be used to improve the apo mat of drinking water.  Thermosetting foams can also be used as molecular sieves, for example, instead of zeolite in an acidic environment in the petroleum industry, because SEOL zeolite is prone to decomposition in this medium, and the foams do not decompose.  By adjusting and cleaning or additional pi.  By rolling the foams, you can obtain the desired micropore size for use as special sieve molecular sieves.  Example 1 5h  concentrated sulfuric acid (parts by weight) are slowly added with stirring to 5 h. -nitroanilin dl. obtain semi-solid paste.  The mixture is slowly heated to 210 ° C until a homogeneous solution is obtained.  Thereafter, a burn reaction occurs with abundant gas evolution, resulting in bulky black pores with a volume expansion of several hundred times compared with the initial volume in the liquid state.  The porous material is then soaked in dilute aqueous HC1 for half an hour and collected again by filtration.  The filter cake is successively washed in water diluted with caustic soda, water, and acetone, re-dispersing in a liquid extract, and re-discharging by filtration.  These steps are necessary to remove all traces of unreacted starting material and fusible condensation products with low molecular weight. weight.  The resulting granules are dried in a vacuum oven overnight at 150 ° C and fired under nitrogen to achieve complete pyrolytic conversion of occluded reagents or intermediates to obtain the required thermoset foam (physiologically inert).  The amount of material emitted is 76% of the total raw material processed.  The elemental analysis for C, H, N, and S corresponds to the formula — h — having several randomly distributed sulfo groups, the number of which decreases depending on the duration of heat treatment at kQQ ° C.  The specific surface area of this material after grinding to 100 mesh.  measured by the indicated BET method using nitrogen at -19b ° C; found to be less than 2m7g.  Example 2  Paste sulfate j-nitroaniline, obtained in example 1, from 5 o'clock  sulfuric acid and k h  C-nitroaniline reacts with, resulting in a voluminous black porous material, which is placed in a cylindrical furnace and heat treated for an additional 6 hours at 250 ° C in nitrogen atmosphere to carry out a complete reaction of the starting materials and remove excess sulfuric acid by dissociation and evaporation.  A small amount of ammonium sulfate, sulfur, and traces of nitroaniline sulfate are recovered in the distillate.  The weight reduction observed during the additional pyrolysis process is due to the removal of water.  The measured surface area is about 5 mu g.  P92 Example Z. The example shows the result of additional pyrolysis of a relatively low-porous black thermoset foam.  A certain amount of black reactive foam obtained in examples 1 and 2 is placed in an oven, maintained at an elevated temperature (see tab. one).  A stream of nitrogen saturated with water at 20 ° C is fed to the foam at a rate of 300 cm / min.  Pyrolysis is continued for 1 hour.  The foam is removed and the specific surface area is measured using a BET method using nitrogen.  Pyrolysis is carried out at 300, 700 and.  It has been found that the specific surface increases with increasing pyrolysis temperature, the weight loss also increases with increasing temperature (see tab. one).  Example +.  1 hour  sodium sulfate is pulverized and mixed with 3 h.  concentrated sulfuric acid, and then from 2 h.   -nitroanil on.  The mixture is heated to with stirring until a homogeneous solution is obtained.  The temperature is slowly increased to 210 ° C, after which the bed reaction begins with the formation of a thermosetting black material with a high porosity, which is soaked in water and re-collected by filtration.  The filter cake was continuously washed with fresh water until the filtrate was free of sulfate ions, as shown by a barium chloride test.  The product is dried overnight in a vacuum oven and then weighed.  Material released is 70% of. theoretical value, based on the structure of polychinoxaline.  Measured specific surface by BET 7 method.  Thus, the addition of a soluble acid salt to the initial mixture leads to the formation of a foam with an increased specific surface.  An example.  phosphoric acid is mixed with 2 hours  i-nitroane. ling and heat to 180 ° C until a homogeneous solution is obtained.  The temperature is slowly increased to 210 ° C, after which the backward reaction begins with the formation of a voluminous black porous material, which is purified as described in Example 1.  The measured specific surface is 670m / g.  The process is repeated with different molar ratios of orthophosphoric acid to α-nitroaniline, resulting in specific surface areas (measured by azo absorption.  at -19b ° C) and the absorption of methylene blue (determined by the usual method) are presented in Table. 2  .  I As can be seen, the resulting surface area and methylene blue absorption depend on the ratios of acid and nitroaniline and reach optimal values with molar ratios between 1.6 and 3.0.  Example 6  7h polyphosphoric acid is mixed with 3 hours.  A-nitroaniline, resulting in a viscous mixture that becomes uniform at.  increase in temperature to.  The temperature of the solution is slowly increased to -210 0, after which a burn reaction occurs with the formation of a black porous material, which is processed as described above.  The specific surface is 300 m / g.  Use phosphoric acid instead of sulfuric acid (see Examples 5 and 6) result in a thermosetting foam with a higher specific: surface, provided that the molar ratio of acid to aromatic compound is in the range of 1.  Example /.  Bh  sulfuric acid is mixed with 4 hours m-nitroacetanilide and the mixture is heated to 210 ° C, resulting in a voluminous black porous material.  Product. treated as described in example I.  Surface area of purified, black thermosetting foam 188 Example 8.  This example shows the sorption and retention capacity of gases on the proposed thermoset foam.  The sorption properties of the foams produced according to the invention are first assessed by degassing small samples under high vacuum conditions, and then by adjusting the absorption of the gas by increased pressure using a device.  The holding capacity is determined first by saturating the Sorbent with sorbate and then pumping it out to constant weight loss at 10 mm Hg. Art.  The specific surface area of the pitch is measured by standard BET methods.  1592 Results for specific gases. listed in Table. Measure the specific surface area and the holding capacity of two types of industrial activated carbon. for different gases, the results of which are presented below.  One type of coal is in a granular state.  All adsorption measurements are made by passing pure gases shown in Table 2 over activated Glam.  From the data in Table 2 it can be seen that the proposed thermosetting foams have a much greater retention capacity of sorbed polar gases and have a retention capacity that increases with increasing specific surface.  Examples  Following the process of Example 1, the nitrogen-containing aromatics shown in Table 1. 5, is subjected to pyrolysis with sulfuric acid with a polar ratio of aromatic compound to sulfuric acid of 1: 2.  It is established that the initial pyrolysis temperature varies slightly from compound to compound, but is in the range of 200-230 ° C.  The results of measurements of specific surface and absorption of methylene blue and iodine (black thermosetting foams) are shown in Table. five.  The specific surfaces are measured by the BET method using nitrogen as indicated in the example. The absorption of methylene oxide and iodine is measured by finding the weight of each of them sorbed by the foams.  High specific surface foams do not always have a large absorption of methylene blue or iodine.  The surface area measured with nitrogen and the uptake of methylene blue and iodine show the distribution of pore size in the foam.  Thus, nitrogen.  is the smallest molecule, iodine is a medium-sized molecule, methylene blue is the largest molecule out of three.  Thus, the values in the table. 5 shows the relative pore sizes and pore size distribution in various foams.  Examples  The process of Example 5 is repeated, except that a number of different aromatic compounds containing nitrogen are listed in Table. 6, is subjected to pyrolysis with phosphoric acid in a weight ratio of 1: 1 (in Example 2, the ratio is 1: 2).  The specific surfaces measured by nitrogen uptake and the uptake of methylene blue and iodine by the resulting foams were measured and are indicated in table. 6  Example 25  The process of the example is repeated using 1 hour.  oxalic acid, 1 h.  sulfuric acid and 1 hour   -nitroaniline.  The surface area of the resulting black foam 280.  Example 26  1h  -nitroaniline and 2 h.  caustic soda is mixed and heated in example 1, to obtain a black porous material with a large pore volume.  It is treated as in example 1 and the specific surface area of the product in example 1 is measured, which is 69.2.  Example 27  Example 2b is repeated, but caustic potassium is used instead of caustic soda.  The surface area of the resulting foam is 163.5 m-g.  The toxicity test of the treated foams according to the invention shows that additional pyrolysis and thorough cleaning results in a non-carcinogenic and non-toxic human foam.  It has been found that severe toxicity (in rats) with the introduction of the material through the mouth is observed when using more than 5000 mg per kilogram of body weight, thus the material is practically non-toxic.  It was also established that death does not occur, there are no pharmacotoxic signs during the study period and there is no large pathology at the autopsy.  In addition, the foam does not cause irritation of the eyes and skin in albino rabbits under study conditions (there are no signs of inflammation of the eyes or skin in any of the experimental animals for the entire study period).  Acute oral toxicity is determined as follows.  Adult albino rats of males and females of the Spragse Dawley breed weighing 150-250 g are not fed for 2k hours, then give them a single calculated dose of foam and are placed in cages with a mesh bottom with free access to. water and laboratory chewing gum (food) for a 2-week observation period.  Method: Served in containers with food.  i Concentration of foam and diluent i (25) in laboratory chewing gum.  17  Sample preparation: Results: Dosing of foam (1) (g / kg) 5 (1) (foam used) Mortality of ddase Vf (2) Day (3) 0/10 during the study 92900518 (2) N death (number ) the period during which deaths were observed.  Dose of oral administration in excess of 5 g / kg.
    ;
    No noticeable changes
    No pharmacotoxic symptoms noted.
    Skin irritation is determined as follows.
    Albino rabbits are placed in separate cells with a mesh bottom and water and gum are ad libitum. Cut the wool from the back and sides of the animal. The test material is applied at two sites of each of the six rabbits. One skinned area and one intact area in the amount of 0.5 ml per area for liquids or 0.5 g per area for solid materials. Treated areas cover with gauze
    BELT and braid to maintain the test material on the skin and reduce the evaporation rate. The animals are put on collars (collars) for 2 hours and for this period they remove their patches and record the degree of erythema and edema according to the following scale. The second reading is taken after 72 hours. The average readings for 24 and 72 hours are used to determine the initial inflammatory mark.
    The concentration of the test material: as indicated.
    Thinner or solvent:
    not.
    No irritation - all readings are negative.
    Initial mark of skin irritation: O
    Scale assessment of skin reaction
    Slight erythema
    Established erythema
    Erythema moderate to severe
    Erythema of a high degree with the formation of a small scab
    Slight edema (barely perceptible)
    Installed edema (definite swelling along edges)
    Eden moderate (swollen area 1 mm)
    Eden severe (swelling more than 1 mm)
    The mark is equal to the sum of the indications of erythema and edema.
    The skin irritation rate is equal to the average of 24 hours, and 72 n marks.
    Glease irritation is determined in the following way.
    Adult albino rabbits of the New Zealand White species wear collars (collars) so that they cannot rub their eyes. 1/10 ml (0.1 g for solids) of the test substance is instilled into one eye and the other eye left as a control without treatment.
    Each substance is used for a group of six albino rabbits. The reaction with the test material is marked according to a grading scale with a violation of the cornea, the iris and the mucous membrane of the eye, which is bulbous and related to the eyelid, 24, 48 and 72 hours after dropping this substance into the eye. The remainder of the test material and accumulated secretion flow out of the eye for a marked time.
    The concentration of the test material: as established.
    Thinner or solvent: no
    Special flushing: no.
    Example 22. Glue is prepared for the production of sheet fiber using pre-treatment with alkaline lignin of Example 9 and an industrial formaldehyde resin. 1400 g of a 25th solution of alkaline lignin are mixed with 375 g of 40 | -phenol-formaldehyde resin and 8225 g of water, having received. solution with a pH of 12.0. Ratio between lignin and 24 h 1 2 3 4 5 6
    phenol formaldehyde on a dry basis 70:30. Thus, it was 20 wt.% Lignin, 8% phenolic resin and 72 wt. water. The adhesive is used to make sheet fiber. Glue is added. fiber slurry for the production of fiber panels. Glue is added to the fiber suspension, after which a solution of aluminum sulphate with a solids content (2) is added to precipitate a solid portion of the resin on the fiber. Solid particles of glue, as well as aluminum sulphate, were reduced to% for dry fiber. Fiber panels are manufactured at 4.69 N / ttZ and pressing time of 5 minutes. The panels are further cured for 4 minutes.
    Properties No irritation - all readings are negative. 24 hour mark. Eye Irritation: O
    No irritation - all readings are negative.
    Mark 48 hours, eye irritation: O
    1 2 3 4 5 6
    No irritation - all readings are negative.
    Mark 72 hours, eye irritation: O Note
    It is established that the use of metal salts of Lewis acid, mixed with at least one aromatic compound containing nitrogen, leads to an increase in the specific surface of the thermosetting foam. It is believed that the metal salt of the Lewis acid can take part in determining the molecular structure of the foam during pyrolysis (as in the case of leaching salts) and have a corrosive effect on thermosetting foam, participating in the formation of additional voids or other. They prefer to use less volatile Lewis acid salts so that they do not disappear during the pyrolysis process. When using metal salts of Lewis acid, only one particular difference is noted; if during additional pyrolysis heating is used, then it should be removed from the foam in advance (as when washing with a solvent). The presence of salt during subsequent processing does not contribute to further processing in order to increase the specific surface.
    Example 28, 2 hours, powdered zinc chloride was thoroughly mixed for 1 hour, 4-nitroaniline, heated to melt, and then stirred for 1 hour. Then the temperature was increased to approximately 210 ° C to stimulate the next reaction stage and suddenly there was no irritation after 1 h after instillation. .2592 formation of a black thermosetting porous material with a large pore volume. This porous material is collected, crushed, washed with dilute hydrochloric acid to leach zinc chloride, and then washed with water (to pH k), diluted with caustic soda, water (to pH 8) and atomic ratio ZnClq p-nitroaniline /
    1.5: 1 2: 1 2.5: 1 3: 1: 1 / by weight
    Methyl Absorption 280 150 Lena Blue, mg / g
    Surface area expressed by the NnI isotherm
    MVr Methyl / 1ene blue absorption is determined by the usual method, and the BET specific surface area, using nitrogen, at -196 ° C. Example 29.2 parts of anhydrous aluminum chloride is mixed with 1 part. A-nitroaniline and the mixture is slowly heated until the start of the exothermic reaction. In this case, the initial heating temperature is 85 ° C. The thermosetting foam is collected and washed thoroughly as described in Example 28, dried at and the uptake of methylene blue, which is 80 mg / g, is measured.
    314-Nitrosophenol
    32 -Nitrosophenol
    33ii-Nitrosophenol 3 -Nitrothiophenol
    50
    25
    950 b | 5
    152
    761
    2k 526 tons, and dried to 80 ° C for 12 hours. It was found that the specific surface of this thermosetting foam depends on the ratio of zinc chloride to 4-nitroaniline, repeat the experiment with different ratios. Example 30. Example 28 is repeated, but anhydrous iron chloride is used instead of zinc chloride. Absorption of methylene blue released by thermosetting foam, but mg / g. P. r and mery. Following the process of Example 28, the following aromatic compounds containing nitrogen and zinc chloride react with the weight ratio indicated below. Consider the results of the measured specific surfaces of the foams obtained, as well as the absorption of methylene blue and yoai.
    . Some foams with high specific surface do not always have a large absorption of methylene blue and iodine. Obviously, the surface area measured with nitrogen and the absorption of methylene blue and iodine indicate the distribution of pore size in the foam. Thus, nitrogen is the smallest molecule, iodine is a medium-sized molecule, and methylene blue is the largest molecule of the three, and thus, the presented values indicate the relative pore sizes and the distribution of pore sizes in different foams.
    Example 41 This example shows the results of pyrolysis at high pressure in a limited environment.
    A-nitroaniline sulfate paste, according to Table 1
    The heat produced in Example 2 ,, is placed in a 1-liter steel bomb under high pressure, which is evacuated before sealing with nitrogen gas to 35 kg / cm. The temperature is gradually increased over 2 hours to a maximum of 220 C with a maximum gas pressure of 66.5 kg / cm2 -. After 1 h at this temperature, the reactor is slowly cooled to room temperature and ventilated. The fragile foam product is carefully washed with dilute sulfuric acid, water and acetone, but in this case no extraction of incompletely reacted nitro compounds is observed. Thus, a more complete conversion to a complete insoluble product can be obtained when the content of the reagents and the product inside the corresponding closed system. The surface area of the purified product is 15.
    T a b l and 15 a 2
    12E 929005
    Continued, table. 2
    600
    HF
    5,600
    30 Continued tabl. 2
    234/760
    20.0
    16,1
    1.3 / 532, 3 7, V532
    3192900532
    Sorbed gas Specific surface holding
    "- - - - - - - - - -------- - - - - - - - - - - --J -
    her 7650.5
    SOft1100 (granulated) 1.1
    HCN1100 (granulated) 0.5
    HjS1100 (granular.) Oh,
    CBq, 7656
    Example Aromatic compound Specific Absorption, mg / g No. Top5 Nitroindolin5152
    5 Nitro-1-naphthylamine 2.5 O
    2-Chloro-yntroanilin1002 4
    2-Methyl-nitroaniline3037
    5 Amino-2-nitrobenzoic
    acid1, k6
    2-amino-4-nitrophenol15 3
    Z-Methyl-4-nitrophenol53
    2-Amino-7-nitrofluoren9b
    1 -Nitrosophenol57,.
    t-Nitrothiophenol22,5
    Table C
    capacity at 23 ° C, weight. ° 4
    Table5
    ness, methylenol lVioda
    . blue sky
    1171 389
    370 356
    33
    权利要求:
    Claims (1)
    [1]
    1. Patent number 362400, cl., 1971 (prototype).
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    同族专利:
    公开号 | 公开日
    GB1475879A|1977-06-10|
    ZA743187B|1975-05-28|
    US4128513A|1978-12-05|
    CA1027924A|1978-03-14|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2469696C2|2006-10-16|2012-12-20|Кэафьюжн 303, Инк.|Vented vial adapter provided with aerosol entrapment filter|US2268419A|1938-10-28|1941-12-30|Us Rubber Co|Antiager|
    US3484387A|1965-05-06|1969-12-16|Burdick & Jackson Lab Inc|Self polymerizable monomers and polymers therefrom|
    US3778336A|1965-09-17|1973-12-11|Scott Paper Co|Heat resistant and oxidation resistant structures|
    US3563917A|1966-01-24|1971-02-16|Research Corp|Quinoxaline polymers|
    US3576769A|1967-05-02|1971-04-27|Monsanto Co|Semicarbonization of thermally stable aromatic polymers|
    US3475374A|1968-02-06|1969-10-28|Research Corp|Quinoxaline polymer compositions|US4236307A|1978-11-02|1980-12-02|Johnson Controls Inc.|Method of making a nitrogen dioxide sensing element|
    US4251375A|1979-04-12|1981-02-17|Pakki Viktor I|Filtering apparatus|
    US4466813A|1982-06-11|1984-08-21|International Business Machines Corporation|Plasticizer removal process and system|
    US4680040A|1986-01-17|1987-07-14|Xerox Corporation|Multipurpose filtering material|
    US4756898A|1987-04-30|1988-07-12|The United States Of America As Represented By The United States Department Of Energy|Low density microcellular carbon or catalytically impregnated carbon foams and process for their prepartion|
    US5226937A|1989-08-18|1993-07-13|Pall Corporation|Void-containing sorbent pad|
    US5354689A|1993-05-10|1994-10-11|The United States Of America As Represented By The Department Of Health And Human Services|Method of detecting isocyanates|
    US6780818B2|1994-02-02|2004-08-24|The Regents Of The University Of California|Quantitative organic vapor-particle sampler|
    AU2002213437C1|2001-10-04|2008-09-04|American Aerogel Corporation|Organic, open cell foam materials|
    US7282466B2|2004-10-04|2007-10-16|The United States Of America As Represented By The Secretary Of The Navy|Sulfur-functionalized carbon nanoarchitectures as porous, high-surface-area supports for precious metal catalysts|
    US9287568B2|2007-04-12|2016-03-15|3M Innovative Properties Company|High performance, high durability non-precious metal fuel cell catalysts|
    US9688933B2|2009-09-11|2017-06-27|The United States Of America, As Represented By The Secretary Of Agriculture|Charcoal-foam heating material|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    GB2518173A|GB1475879A|1973-05-25|1973-05-25|Sorbent thermoset foam materials|
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