![]() Process for producing anthraquinonesulfamides
专利摘要:
公开号:SU932984A3 申请号:SU802968552 申请日:1980-08-21 公开日:1982-05-30 发明作者:Риджэрд Рэнделл Дональд;Филлипс Эмир 申请人:Циба-Гейги Аг (Фирма); IPC主号:
专利说明:
The invention relates to a process for the preparation of new compounds of anthraquinone sulfamides, which can be used as catalysts for the purification of gases from hydrogen sulfide. Anthraquonone disulfonic acids are known, in particular, 2,7-anthraquinondysulfokispot, which is a catalyst for gas purification from hydrogen sulfide. The purpose of the invention is to obtain new compounds with a higher hydrogen sulfide activity than the known compound. The goal is achieved by the method of obtaining anthraquinone sulfamides of the general formula OG KA-B (I) where a is B - SOgH; M - alkali metal, 20 R - hydrogeni R is hydrogen or alkali metal, based on a known reaction of reacting an aromatic amine with an alcohol at elevated temperatures. 2S Round 2, which implies that anthraquinonsulfonamide of the general formula </ BR> where R and R are the indicated values, interact with the compound of the general formula </ BR> where A and B have the indicated values in an alkaline medium. The process is carried out by heating to 100 ° C. The average duration of the process is 1-12 hours. The preferred temperature is 60-80 ° C. Sodium hydroxide is used as an alkaline medium. The compounds of III are obtained from formaldehyde and sodium bisulfite in aqueous solution at 80 ° C. Under the conditions of the proposed method, the following compounds are the most active: N, N-bis-sulfomethyl-anthraquinone-2, 6-disulfonamide, M, N-bis-sulfosulfonthraquinone-2,7-disulfonamide or a mixture of these compounds in any ratio. Example 1. 76.9 g of sodium formaldehyde bisulfite and 22.9 g of sodium hydroxide in 300 g of water are placed in a three-necked flask equipped with a bottle, a thermometer and a refrigerator, and the solution is heated to 70 sec. I05 g of mixture 1 is added in portions: 1 anthraquinone-2,6 / 2,7-disulfonamides, and the mixture is heated at 70 for 3 hours. After evaporation of the resulting solution, 171.4 g of N, N-disulfomethyl anthraquinone-2,6 / 2,7- disulfonamidov dark brown, so pl. vpepe Elementary Consultation,%: C 25.9; H 2.2; N 4.1; S 17.7; Na 13.2 SG 0.1,, 9; water 5.4. Example2. 4 g of sodium formaldehyde bisulfite and 1.2 g of sodium hydroxide in 20 g of water are treated with 5.6 g of anthraquinone-2,7-disulfonamide, as described in example 1. After evaporation of the resulting solution, 6.5 g of sodium salt of M, N-disulfomemilanthraquinone are obtained -2, 7-disulfonamida dark brown, so pl. above 250 C. Elementary composition,%; C 16.3; n 2.3; N 3,6; S 19, Na 14.4; , 1, 4.0. Example 3.7 g of sodium formaldehyde sulfide and 1.1 g of sodium hydroxide in 20 g of water are treated with 5 g of anthraquinone-1,5-disulfonamide, as described in the example,. After evaporation of the resulting solution, 6.5 g of sodium salt N are obtained. - Disulfomethylanthraquinone-1,5-disulfonamide black, tlsh. over 300 ° C. Elementary composition,%:, 2, Н2,1; N3.7, S 18, 15.5; , his, 9, -, 9, water 8.2. Example 4. 6.1 g of sodium phosphate bisulfite and I, 8 g of sodium hydroxide in 40 g of water are treated with 8.4 g of a mixture of anthraquinone-1,6 / 1,7-disulfonamides, as described in example 1. After evaporation of the resulting solution, 15 are obtained , 1 g of sodium salts of N, N-disulfomethylanthraquinone-1, 6 / 1,7-disulfonamides black, so pl. higher than 300 ° C. Elementary composition,%: C 26, 1; H 2.1u N 3.6, S 17.99; Na 13.3; CSF, 4; S0 15.9, water 6.7. When potassium formaldehyde bisulfite is used in examples 1-4, the corresponding tetrapotassium salts are obtained. Similarly, using ammonium formaldehyde bisulfite and ammonium hydroxide, tetraammonium salts are obtained. The activity of the compounds of formula (1) is determined in comparison with 2,7-anthraquinone sulfonic acid (2.7-ADC) pTj A simulating gas absorption is prepared for conducting the experiments: 1 solution of the following composition, g / l: sodium bicarbonate 25 sodium sodium carbonate 5 sodium thiosulfate 10 Rodanide sodium 8 vanadate sodium 3.8 Catalyst2 pH of test solution9, 0-9.2. The test chamber is a 1-liter vessel containing an oxygen electrode, a compensated temperature sensor, a calomel electrode, a platinum electrode, an air inlet, and a valve sintered disk. The content of dissolved oxygen is measured using an EIL system for measuring dissolved oxygen, and the oxidation-reduction potential is measured using a universal high-resistance electrical measuring instrument. The parameters characterizing the efficiency of the catalytic system are as follows: 20% of the time for which the content of the dissolved acid / hydroxide in the solution reaches 20% of the total content, time during which contain / about the solution of dissolved oxygen in the solution reaches 80% of the total content of the surface; the ratio Eg / E, where Eg is the redox potential of the system in the fully reduced state, and E is the redox potential of the system in the oxidized state. For convenience, we have taken in our experiments, which is the redox potential at apo / The results in the table are average for three reduction and re-oxidation cycles. The table compares 2,7-anthraquinone disulfonic acid (ADC) with the following E1 compounds and mixtures of compounds: A - chetyryodsatrivye Y, N-disulfomethylangraquinone-2, 6/2, 7-disulfonamid.J F is the four-sodium salt of M, M-di sulfomethylanthraquinone-2,7-disulfonamide. G is the four-sodium salt of M, M-disulfomethylanthraquinone-I, 5-disulfonamide. H - tetrasodium salts of M, M-disulfomethylanthraquinone-1, 6 / 1,7-disulfonamides. Some of the reactions that bind oxygen gas in solution are ionic in nature and proceed relatively quickly. Usually, while ionic compounds in a reduced state are present in a solution, the content of dissolved oxygen is maintained at 5% or less of the total dissolved oxygen in the liquid. Therefore, it is possible to determine whether these compounds are in a reduced or oxidized state in solution by measuring the content of generated oxygen. Therefore, the re-oxidation time trtjyj, and QQO / indicate the re-oxidation rate in the presence of various catalysts. Since the process is oxidative, it depends on redox pairs. The degree of oxidation of the solution determines the redox potential. Thus, the degree of oxidation is measured continuously by measuring the redox potential. The liquid consists of at least three redox pairs. The potential of an individual electrode is logarithmically O with the concentration of oxidized and reduced groups in solution. Not potential standard con11, concentration al + constant x log concentration 5 forms reduced forms The ratio is determined by other workers to indicate the degree of re-oxidation. The efficiency of the catalyst can be determined by considering the values of the content of dissolved oxygen and the redox potential. Results, . usually obtained in a test chamber, can be divided into three main types i - long duration of reaching 120 (for example, 30 minutes or more), but a high ratio Ec / Ei 0 / l l 3 I and example 2.2 or more; P - average duration of reaching t2oo / (for example, about 0 min) and a high degree (for example, 2.2 or more); 5 ii - quick achievement (for example, 1-3 minutes), but low Eg / Ei ratio (for example, less than 2.0) The interpretation of these results is as follows: Type I is a slow but effective catalyst, type P is an effective catalyst, type Ш - inefficient catalyst, 5 When the dissolved oxygen content in the solution reaches 20% of the saturation content, most of the redox reaction has already occurred. The solution contains a lot of dissolved oxygen, therefore, the time of 20% D ° 1 dots is mainly a function of the activity of the catalyst. Therefore, the smaller the time interval 5 between, and tgg, the easier the catalyst is oxidized again and - provided that the ratio is. more than 2.2 the more effective catalyst in the system. Comparison of the activity of hydrogen sulfide compounds of formula 1 with ADC Q Compare 2.7-ADC to function l | j Examples 10-14. A 5 l simulating gas absorption solution is prepared, and 5 l of this solution is loaded into the chamber. Then the solution is washed three times with oxygen, followed by the removal of oxygen from it. This is done by alternately passing through a solution of air and nitrogen at a rate of 500 ml / min. At the end, the solution is left in an oxygen-free state. The minimum amount of dissolved oxygen-free solution is selected to dissolve 3.75 g of sodium sulfide, then this solution is reintroduced into the chamber. Although the process is carried out in order to remove the hydrogen sulfide, however, when the hydrogen sulfide is dissolved in the alkaline solution, HS-ions are formed. Therefore, it was decided that dp is convenient for conducting experiments, introducing HS-ions using sodium sulfide. The S-ion formed from sodium sulfide forms the H5 -ion at the pH of the simulating solution of the getter solution. After the reduction of sodium sulfonates, a weak stream of nitrogen is passed through for 10 minutes, ensuring the stirring of the solution, the stabilization of the redox potential, and the content of dissolved oxygen. Then the BHOBt solution is saturated with oxygen by -430 -197 2.2 2.4 2.5 4.5 2.7 air flow at 500 ml / min. The content of dissolved oxygen and the redox potential of continuous but register. Oxidation is continued until the establishment of a constant redox potential and dissolved oxygen content. After this solution it is deaerated by passing nitrogen at a rate of 500 ml / min, then reduced by the addition of 3.75 g of sodium sulfide. Reduction with additional sodium sulfide followed by re-oxidation — by passing air (when measuring the content of dissolved oxygen and redox potential) is produced three times and the sulfur intake is filtered off after each cycle. The results are shown in the table. As can be seen from table1, Formulas (1) are of the type: (1 and their activity exceeds the activity of 2.7-ADC, i.e. the higher the ratio Eg / E, the more active the catalyst. In the case of the proposed compounds, this ratio is 2.4- 4.5, and in the well-known - 2.7 ADC - 2.2 with the same time interval between t 80 / o
权利要求:
Claims (2) [1] Invention Formula The method of producing anthraquinone sulfamides of general formula E.T 1 To B-A-COGG-A-b (I) A B M , alkali metal R r -hydrogen; - hydrogen or alkali metal. About the fact that, anthraquinonsulfamid general formula P OzIHBl EKKOg 5 1 where R - have the indicated meanings, are reacted with a compound of the general formula III NOAV where L and B have the indicated meanings, in an alkaline medium. Sources of information taken into account in the examination I. Patent of Great Britain No. 871233,. From 01B publish. 1961.. [2] 2. Vorozhtsov N.N. Basics of synthesis of intermediate products and dyes. M., Goskhimizdat, 1955, p. 696.
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引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 US2132169A|1935-10-11|1938-10-04|Agfa Ansco Corp|Photographic desensitizing| US2131742A|1935-10-11|1938-10-04|Agfa Ansco Corp|Photographic desensitizing| US2163146A|1936-10-07|1939-06-20|Agfa Ansco Corp|Taurides| DE935987C|1951-10-18|1955-12-01|Sandoz Ag|Process for the preparation of sulfonic acid amides of the anthraquinone series| US2938914A|1957-09-25|1960-05-31|American Cyanamid Co|Alkyl trialkylammonium salts as disperse dyes for acrylic fibers| US2997439A|1959-05-14|1961-08-22|North Western Gas Board|Removal of hydrogen sulphide from hydrocarbons with anthraquinone disulfonic acids| NL252378A|1959-10-21| NL270089A|1960-10-12| US3627791A|1968-11-21|1971-12-14|Richardson Merrell Inc|Bis anthraquinones| DE2135022A1|1971-07-14|1973-01-25|Richardson Merrell Inc|Bis anthraquinones - useful as antiviral agents| JPS5076842A|1973-11-07|1975-06-23| JPS5092294A|1973-12-18|1975-07-23| GB1505996A|1974-08-27|1978-04-05|British Gas Corp|Gas purification liquors| US4251493A|1978-07-21|1981-02-17|Ciba-Geigy Corporation|Gas purification process|US4251493A|1978-07-21|1981-02-17|Ciba-Geigy Corporation|Gas purification process| US4432962A|1979-06-20|1984-02-21|Union Oil Company Of California|Method for removing hydrogen sulfide from gas streams| JPS5840386A|1981-06-30|1983-03-09|Union Carbide Corp|Manufacture of low sulfur high quality coke from high sulfur decant oil| FR2512687B1|1981-09-11|1984-04-20|Raffinage Cie Francaise| EP0147364A1|1983-10-26|1985-07-03|Ciba-Geigy Ag|Process for removal of hydrogen sulphide from gases| GB2166453B|1984-08-01|1987-10-28|Ciba Geigy Ag|Purification process| US5017480A|1987-08-10|1991-05-21|Ajimomoto Co., Inc.|Process for recovering L-amino acid from fermentation liquors| JPH05124671A|1991-10-24|1993-05-21|Nec Data Terminal Ltd|Locking device for opening and closing cover| AUPR229600A0|2000-12-22|2001-01-25|Commonwealth Scientific And Industrial Research Organisation|New oxygen scavenging compositions| WO2008140792A1|2007-05-10|2008-11-20|Avalon Pharmaceuticals|Derivatives of fluorene, anthracene, xanthene, dibenzosuberone and acridine and uses thereof|
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