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System for preparing 1-amino-8-naphthol-4,6-disulfonic acid

A technology of disulfonic acid and amino group, applied in the field of chemical industry, can solve the problems of destructive enhancement of natural resources, large industrial energy consumption, backward management level, etc., and achieves reduction of raw material cost and consumption, energy saving and emission reduction of process conditions, and optimization of production process. Effect

Inactive Publication Date: 2015-08-26
枣庄博胜活性钙有限公司
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Problems solved by technology

The serious impact of the current global financial crisis is that the industrial structure is unreasonable, and the industry is concentrated in labor-intensive products; technology-intensive products are obviously lagging behind developed industrial countries; the decisive role of production factors is gradually weakening; industrial energy consumption is large, output rate is low, Serious environmental pollution and increased destructiveness to natural resources; the overall scale of enterprises is relatively small, insufficient technological innovation capabilities, and backward management levels, etc.

Method used

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  • System for preparing 1-amino-8-naphthol-4,6-disulfonic acid

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Embodiment Construction

[0015] Such as figure 1 A system for preparing 1-amino-8-naphthol-4,6-disulfonic acid is shown, which includes a raw material storage tower 1, a first synthesis reaction tower 2, a second synthesis reaction tower 3, and a filtration reaction tower 4. The first centrifugal reaction tower 5, the third synthesis reaction tower 6, the acidification reaction tower 7, the fourth synthesis reaction tower 8, the decolorization reaction tower 9, the dilution reaction tower 10, the second centrifugal reaction tower 11, the waste water collection tank 12 , Wastewater treatment system 13, sulfuric acid storage tank 14, ammonia water storage tank 15, intermediate reaction tank 16, potassium chloride solution storage tank 17, finished product storage tank 18; among them, the discharge port of the raw material storage tank 1 is connected to the first In the inlet of the synthesis reaction tower 2, dissolve 2-naphthol in 98% sulfuric acid at 60 degrees Celsius, react for 6 hours, and then add ...

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Abstract

The invention discloses a system for preparing a 1-amino-8-naphthol-4,6-disulfonic acid. The system comprises a raw material storage tower, a first synthesis reaction tower, a second synthesis reaction tower, a filtering reaction tower, a first centrifugal reaction tower, a third synthesis reaction tower, an acidifying reaction tower, a fourth synthesis reaction tower, a decolorizing reaction tower, a dilute reaction tower, a second centrifugal reaction tower, a wastewater collection tank, a wastewater treatment system, a sulfuric acid storage tank, an ammonium hydroxide storage tank, an intermediate reaction tank, a potassium chloride solution storage tank and a finished product storage tank. The 1-amino-8-naphthol-4,6-disulfonic acid product prepared by the system is high in purity; the purity is greater than 95.3%; the H acid content is smaller than or equal to 1.5%; and the content of an insoluble matter is smaller than or equal to 0.1%.

Description

Technical field [0001] The invention relates to a system for preparing 1-amino-8-naphthol-4,6-disulfonic acid, which belongs to the chemical industry field. Background technique [0002] K acid, gamma acid, Tobias acid, J acid, etc. are all downstream products of 2-naphthol. Most of their production processes involve typical chemical production processes such as sulfonation, neutralization, acidification, and ammoniation. The industrial production methods for products such as K acid, gamma acid, Tobias acid, and J acid are relatively simple. The production of K acid is based on 2-naphthol as the main raw material. It is monosulfonated in anhydrous methanol and sulfuric acid according to a certain ratio of ingredients in a sulfonation pot to obtain 2-naphthol-6.8-disulfonic acid. , And then react with KCl in the salting-out kettle to obtain G salt. After the G salt and ammonia are ammoniated in the ammoniating kettle, they are then subjected to acid precipitation in the acidic p...

Claims

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Application Information

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IPC IPC(8): C07C309/50C07C303/22
Inventor 李平兰
Owner 枣庄博胜活性钙有限公司
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