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

A disulfonic acid and amino technology, applied in the chemical industry, can solve the problems of increased destructiveness of natural resources, large industrial energy consumption, backward management level, etc., and achieve reduction of raw material costs and consumption, energy saving and emission reduction of process conditions, and optimization of production processes Effect

Inactive Publication Date: 2016-06-22
枣庄博胜活性钙有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

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

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Embodiment Construction

[0015] Such as figure 1 Shown is a system for preparing 1-amino-8-naphthol-4,6-disulfonic acid, 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 color removal 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 storage tank 15, intermediate reaction tank 16, potassium chloride solution storage tank 17, finished product storage tank 18; wherein, the outlet of raw material storage tank 1 is connected to the first The feed inlet of synthesis reaction tower 2, 2-naphthol is dissolved in 98% sulfuric acid at 60 degrees centigrade, reacts for 6 hours, then adds fuming sulfuric ac...

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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 field of chemical industry. Background technique [0002] K acid, gamma acid, tunic 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 of products such as K acid, gamma acid, tunic acid, J acid are relatively single. The production of K acid is based on 2-naphthol as the main raw material, in anhydrous methanol and sulfuric acid according to a certain proportioning ratio, through a sulfonation pot, for monosulfonation, sulfonation to obtain 2-naphthol-6.8-disulfonic acid , and then react with KCl in the salting-out kettle to obtain G salt. After being ammoniated in the ammoniation kettle, the G salt and ammonia water are then subjected to acid analysis...

Claims

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Application Information

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