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A kind of treatment method of waste acid water

A treatment method and technology for waste acid water, which are applied in multi-stage water treatment, multi-stage water/sewage treatment, biological water/sewage treatment, etc., which can solve the need for desulfurization treatment of exhaust gas, high equipment quality requirements, and large investment in environmental protection treatment. and other problems, to achieve the effect of reducing energy consumption, short processing flow and less equipment

Active Publication Date: 2020-09-15
CHONGQING UNISPLENDOUR CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The ACH method is characterized by the effective use of petrochemical by-product HCN, and the high yield of MMA. At the same time, with the continuous improvement and perfection of the process, its production advantages are more obvious, but the process still has the following disadvantages: process production has by-product waste acid Water, which is highly acidic, requires high quality equipment; the process of using waste acid water to recover by-product ammonium sulfate is complicated, resulting in relatively large investment in subsequent environmental protection treatment of condensate and waste gas
[0006] (2) The amount of organic light mother liquor is 0.4-0.5t / t, and 10-20% of ammonium sulfate is entrained, causing SO in the tail gas of waste liquid incineration 2 The content is as high as 8000-10000ppm, resulting in the need for desulfurization treatment of tail gas;
[0007] (3) Waste acid water contains 0.1% MMA, 0.5% methanol, 0.1% acetone, 0.4% methacrylic acid sodium salt, 5.5% methacrylic acid polymer, 0.3% methacrylic acid and methacrylic acid oligomer substances, a small amount of α-hydroxyisobutyric acid, acetone monosulfonic acid, acetone disulfonic acid, etc. During the neutralization of these organic substances with ammonia, the acidic organic substances will generate corresponding ammonium salts, but high polymers, oligomers Organic substances such as acetone, methanol, and MMA overflowed from the upper part of the reactor, entraining a large amount of ammonium sulfate solution; some organic substances dissolved in the reaction solution also affected the crystallization of ammonium sulfate;

Method used

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Examples

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Embodiment 1

[0026] A method for treating waste acid water, wherein, the waste acid water is the waste acid water produced in the process of preparing methyl methacrylate by the ACH method, and the waste acid water contains 33.21% water and 14.02% sulfuric acid in percent by mass. %, ammonium bisulfate 45.50%, MMA 0.1%, methanol 0.5%, acetone 0.1%, methacrylic acid sodium salt 0.4%, methacrylic acid polymer 5.5%, methacrylic acid and methacrylic acid oligomer 0.3% , a small amount of α-hydroxyisobutyric acid, acetone monosulfonic acid, acetone disulfonic acid, etc.; specifically follow the steps below for intermittent operation:

[0027] Before the reaction, feed a small amount of water into the reactor, then add part of the waste acid water, and then continuously feed the remaining waste acid water and all the ammonia gas to control the pH at the end of the reaction to 6.0; the gas coming out of the top of the reactor is directly Pass it into the middle of the rectification tower for rect...

Embodiment 2

[0030] A method for treating waste acid water, wherein, the waste acid water is the waste acid water produced in the process of preparing methyl methacrylate by the ACH method, and the waste acid water contains 33.21% water and 14.02% sulfuric acid in percent by mass. %, ammonium bisulfate 45.50%, and a small amount of organic matter; it specifically performs intermittent operation according to the following steps, and its technological process diagram is attached figure 2 Shown:

[0031] Before the reaction, feed a small amount of water into the reactor, then add part of the waste acid water, and then continuously feed the remaining waste acid water and all the ammonia gas to control the pH at the end of the reaction to 6.0; the gas coming out of the top of the reactor is directly Pass it into the middle of the rectification tower for rectification separation, control the temperature of the tower bottom to 130°C, and the temperature of the tower top to 30°C; send the high-conc...

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Abstract

The invention relates to a waste acid water treating method. Waste acid water is produced in the process of preparing methacrylic acid or methacrylate substances by adopting an ACH method. The waste acid water treating method is characterized in that the waste acid water and ammonia gas are added into a reactor to perform intermittent reaction, so that the ammonia gas is completely absorbed, and gas out of the top of the reactor is directly used for rectification and separation. The waste acid water treating method has the multiple advantages of being short and simple in treatment process, easy to operate and low in investment cost and adopting few devices.

Description

technical field [0001] The invention relates to the treatment of by-product waste acid water in the production of methyl methacrylate, in particular to a treatment method of waste acid water. Background technique [0002] Methyl methacrylate (MMA) is an important organic chemical raw material, mainly used in the field of polymerization and copolymerization, and is the most important chemical industry product among methacrylates. The application of MMA covers all aspects of society, involving construction, electronics, medical care, aerospace, automobiles and other fields, and its demand is increasing, especially in the pursuit of high-performance polymer materials, methyl methacrylate materials are in huge demand and become R&D hotspots. [0003] At present, the production methods of MMA mainly include ACH method, isobutylene method and ethylene method. As a traditional and mature production process, the ACH method is the most widely used in the world, accounting for 75% o...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F1/66C02F9/14C01C1/242F23G7/04
CPCC01C1/242C02F1/38C02F1/66C02F3/00C02F9/00C02F2101/101C02F2301/08F23G7/04F23G2209/101
Inventor 柳亚玲连许帅郑道敏王玉飞姚如杰金海琴
Owner CHONGQING UNISPLENDOUR CHEM
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