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Recovery method of naphthalene in production of efficient naphthalene water reducing agent and required system thereof

A high-efficiency water-reducing agent and naphthalene recovery technology, applied in chemical instruments and methods, hydrocarbons, organic chemistry, etc., can solve the problems of long contact time between materials and hot steam, insufficient recovery rate, long recovery time, etc. The effect of low cost, short recovery period and high recovery rate

Inactive Publication Date: 2012-08-08
辽宁岩砂晶建材有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002]Naphthalene-based water reducer is made of industrial naphthalene through sulfuric acid sulfonation, hydrolysis, formaldehyde condensation, and lye neutralization. The biggest one is that naphthalene accounts for more than 60% of its production cost, and the reaction rate of naphthalene is generally about 80%, and the unreacted 20% naphthalene is not recycled by most manufacturers, so the recovery of naphthalene is of great significance, and the utilization rate of naphthalene In other words, the recovery rate has become a major issue in the production of naphthalene-based high-efficiency water reducers, and it is also an important means to improve product competitiveness. A small number of manufacturers use steam distillation to recover naphthalene, but the recovery time is long and the recovery rate is low. It is not high enough, and the material is easy to decompose for a long time in contact with hot steam. Therefore, it is of great practical significance to find a new method and equipment for recovering naphthalene with high efficiency.

Method used

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  • Recovery method of naphthalene in production of efficient naphthalene water reducing agent and required system thereof
  • Recovery method of naphthalene in production of efficient naphthalene water reducing agent and required system thereof
  • Recovery method of naphthalene in production of efficient naphthalene water reducing agent and required system thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] The naphthalenesulfonic acid hydrolyzate in the naphthalenesulfonic acid hydrolysis kettle passes through the first film evaporator 1 (first-stage falling film evaporator) at a speed of 30kg / min, and the azeotrope of naphthalene and water is condensed by the condenser and enters the first The naphthalene receiving filter 10 (receiving tank) can be recovered, and the material after falling film evaporation and removal of naphthalene in the first thin film evaporator 1 enters the second fluidized film evaporator 3 (secondary fluidized evaporator), and the naphthalene is removed for the second time. The material after the second removal of naphthalene enters the condensation tank for condensation reaction. The system pressure is 0.04MPa and the temperature is 98 degrees. The naphthalene removal time of each kettle material is 100 minutes.

Embodiment 2

[0049] The naphthalenesulfonic acid hydrolyzate in the naphthalenesulfonic acid hydrolysis kettle passes through the first film evaporator 1 (first-stage falling film evaporator) at a speed of 33kg / min, and the azeotrope of naphthalene and water passes through the condenser and enters the first The naphthalene receiving filter 10 (receiving tank) can be recovered, and the material after falling film evaporation and removal of naphthalene in the first thin film evaporator 1 enters the second fluidized film evaporator 3 (secondary fluidized evaporator), and the naphthalene is removed for the second time. The material after the second removal of naphthalene enters the condensation tank for condensation reaction. The system pressure is 0.037MPa and the temperature is 96 degrees. The naphthalene removal time of each kettle material is 90 minutes.

Embodiment 3

[0051] The naphthalenesulfonic acid hydrolyzate in the naphthalenesulfonic acid hydrolysis kettle passes through the first film evaporator 1 (first-stage falling film evaporator) at a speed of 37kg / min, and the azeotrope of naphthalene and water passes through the condenser and enters the first The naphthalene receiving filter 10 (receiving tank) can be recovered, and the material after falling film evaporation and removal of naphthalene in the first thin film evaporator 1 enters the second fluidized film evaporator 3 (secondary fluidized evaporator), and the naphthalene is removed for the second time. The material after the second removal of naphthalene enters the condensation tank for condensation reaction. The system pressure is 0.035MPa and the temperature is 94 degrees.

[0052] The naphthalene removal time of each kettle material is 80 minutes.

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Abstract

Belonging to the technical field of concrete admixture production, the invention especially relates to a recovery method of naphthalene in production of an efficient naphthalene water reducing agent and a system thereof. The naphthalene recovery method comprises: placing a naphthalene sulfonic acid hydrolysate into a first film evaporator (1), and controlling the temperature and vacuum degree to make naphthalene and water form an azeotrope, which is sent into a first naphthalene reception filter (10) for recovery. The naphthalene recovery system consists of: a first film evaporator (1), a naphthalene sulfonic acid hydrolysis kettle (2), a first condenser, a first naphthalene reception filter (10) and a vacuum pump (12). A condensation outlet (102) of the first film evaporator (1) is communicated with a condensation medium inlet (501) of the first condenser; the condensed naphthalene outlet (503) is communicated with a raw material inlet of the first naphthalene reception filter (10); and a vacuum interface of the first naphthalene reception filter (10) is communicated with the vacuum pump (12). The system of the invention has the advantages of simple operation, high recovery rate, good material stability and low cost.

Description

Technical field [0001] The present invention is the field of concrete exterior production technology, especially in the production method and its required systems in the production of an efficient water reduction agent. Background technique [0002] The water reducing agent is made of industrial 萘 sulfate, hydrolysis, formaldehyde contraction, and alkaline liquid neutralization.The response rate is generally around 80%, and most of the 20%of the unresponsive manufacturers are not recycled. Therefore, the recycling of 萘 is of great significance.A major topic is also an important means to improve product competitiveness. A small number of manufacturers adopt the method of recycling the method of water vapor distillation.Therefore, the method and equipment to seek a new high -efficiency recycling 萘 have significant practical significance. Invention content [0003] The present invention aims to overcome the shortcomings of existing technology and provide a high recycling method wit...

Claims

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Application Information

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IPC IPC(8): C07C15/24C07C7/00
Inventor 黄海滨黄海忠黄丽佳
Owner 辽宁岩砂晶建材有限公司
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