Summary of the invention:
In order to overcome above-mentioned traditional technology preparation method's shortcoming, the invention provides a kind of 2,4-dinitrobenzene sulfonic acid sodium hydrogenation preparing 2, the technology of 4-diamino benzene sulfonic acid sodium, for achieving the above object, the present invention adopts following scheme:
2,4-dinitrobenzene sulfonic acid sodium is dissolved in the solvent, solvent is water or low-carbon alcohol, add catalyzer, hydrogenation reaction, when adding hydrogen in the reactor hydrogen pressure be controlled at 0.1 ~ 2.5MPa, temperature of reaction kettle is controlled at 35 ℃ ~ 150 ℃ when adding hydrogen, catalyzer is palladium charcoal or Ni-Al alloy catalyst, and catalyst levels is the 1-10% of the quality of reactant, and reaction equation is as follows:
Generate 2 earlier, 4-diamino benzene sulfonic acid sodium reaction solution removes by filter catalyzer, and activated carbon decolorizing is removed impurity, and concentrated post crystallization separates out 2, and 4-diamino benzene sulfonic acid sodium is produced sour body as need, and then transferring PH with hydrochloric acid is 2, and crystallization separates out 2, the 4-diamino benzene sulfonic acid.
Of the present invention a kind of 2, the preparation technology of 4-diamino benzene sulfonic acid sodium has following effect or advantage:
1. reduced production cost;
2. whole process of production does not have waste water discharge, no spent acid emission problem, more compliance with environmental protection requirements.
Embodiment
Embodiment 1: in the 1000ml autoclave, add entry 500ml, 2,4-dinitrobenzene sulfonic acid sodium 176.5g (content 85%), palladium carbon catalyst 5g, airtight autoclave is evacuated down to earlier-0.095MPa, charging into nitrogen 1MPa. again repeats 3 ~ 5 times, at last system is evacuated, reaction solution is heated to 50 ℃, begins logical hydrogen, pressure is 1 ~ 1.6MPa, control reaction temperature is at 50 ~ 100 ℃, and hydrogen pressure no longer reduces in reactor, cooling, open autoclave after the emptying, remove by filter the palladium charcoal, use the 10g activated carbon decolorizing, be concentrated to original volume 1/3rd, the cooling post crystallization goes out 2,4-diamino benzene sulfonic acid sodium 115g.Content 82.6%, yield 81.42%.
Embodiment 2: in the 1000ml autoclave, add entry 500ml, 2,4-dinitrobenzene sulfonic acid sodium 176.5g (content 85%), palladium carbon catalyst 2g, airtight autoclave, be evacuated down to earlier-0.095MPa, charge into nitrogen 1MPa. again and repeat 3 ~ 5 times, at last system is evacuated, reaction solution is heated to 50 ℃, begin logical hydrogen, pressure is 1 ~ 1.6MPa, and control reaction temperature is at 50 ~ 100 ℃, and hydrogen pressure no longer reduces in reactor, cooling, open autoclave after the emptying, remove by filter the palladium charcoal, the mother liquor after filtering among the embodiment 1 is poured into, add the 10g activated carbon decolorizing, solution concentration is to original volume 1/3rd, and the cooling post crystallization goes out 2,4-diamino benzene sulfonic acid sodium 133g.Content 82.3%, yield 93.82%.
Embodiment 3: feed intake reaction and aftertreatment be with embodiment 2, be concentrated to original volume 1/3rd after, transfer about PH=2 with 30% hydrochloric acid, decrease temperature crystalline goes out 2,4-diamino benzene sulfonic acid, weight 106g behind the suction filtration.Content 92.4%, yield 94.18%.
Embodiment 4: in the 1000ml autoclave, add entry 150ml, ethanol 400ml, 2,4-dinitrobenzene sulfonic acid sodium 176.5g (content 85%), palladium carbon catalyst 3g, airtight autoclave, reaction solution is heated to 50 ℃, begin logical hydrogen, pressure is 0.8MPa, exothermic heat of reaction, 80 ℃ of temperature controls, pressure 1 ~ 1.2MPa inhales hydrogen and no longer changes to pressure, cools to below 50 ℃, emit reaction solution, filter, remove catalyzer, be concentrated to 1/3rd of original volume after the decolouring, the cooling post crystallization goes out 2,4-diamino benzene sulfonic acid sodium 136g.Content 82.6%, yield 96.28%.
Embodiment 5: in the 1000ml autoclave, and ethanol 520ml, 2,4-dinitrobenzene sulfonic acid sodium 176.5g (content 85%), palladium carbon catalyst 4g, airtight autoclave, reaction solution are heated to 50 ℃, begin logical hydrogen, pressure is 0.8MPa, exothermic heat of reaction, 80 ℃ of temperature controls, pressure 1.6 ~ 1.8MPa inhales hydrogen and no longer changes to pressure, cools to below 50 ℃, emit reaction solution, filter, remove catalyzer, be concentrated to 1/3rd of original volume after the decolouring, the cooling post crystallization goes out 2,4-diamino benzene sulfonic acid sodium 138g.Content 82.2%, yield 97.21%.
Embodiment 6: in the 1000ml autoclave, methyl alcohol 460ml, 2,4-dinitrobenzene sulfonic acid sodium 176.5g (content 85%), Ni-Al alloy catalyst 4.5g, airtight autoclave, reaction solution are heated to 50 ℃, begin logical hydrogen, pressure is 0.8MPa, exothermic heat of reaction, 80 ℃ of temperature controls, pressure 2 ~ 2.2MPa, inhaling hydrogen no longer changes to pressure, cool to below 50 ℃, emit reaction solution, filter, remove catalyzer, be concentrated to 1/3rd of original volume after the decolouring, the cooling post crystallization goes out 2,4-diamino benzene sulfonic acid sodium 132g.Content 82.4%, yield 93.22%.
Embodiment 7: in the 1000ml autoclave, Virahol 400ml, 2,4-dinitrobenzene sulfonic acid sodium 176.5g (content 85%), Ni-Al alloy catalyst 3g, airtight autoclave, reaction solution are heated to 50 ℃, begin logical hydrogen, pressure is 0.8MPa, exothermic heat of reaction, 80 ℃ of temperature controls, pressure 2.2 ~ 2.5MPa, inhaling hydrogen no longer changes to pressure, cool to below 50 ℃, emit reaction solution, filter, remove catalyzer, be concentrated to 1/3rd of original volume after the decolouring, the cooling post crystallization goes out 2,4-diamino benzene sulfonic acid sodium 135g.Content 83.2%, yield 96.25%.
Illustrate: palladium carbon catalyst is applied mechanically 50 times continuously, and its activity does not descend substantially.