Production method and system for co-production of acetyl chloride by 1-hydroxyethylidene-1,1-diphosphonicacid

A technology of hydroxyethylene diphosphoric acid and its production method, which is applied in the field of co-production of acetyl chloride by hydroxyethylene diphosphoric acid, can solve the problem that it is difficult to realize the dynamic adjustment of HEDP and acetyl chloride, increase the difficulty of recovering acetic acid, and the inability to directly produce acetic acid containing water. Use and other problems to achieve the effect of reducing operation difficulty and labor intensity, high energy consumption and long time consumption

Inactive Publication Date: 2016-06-01
天津科维津宏环保科技有限公司 +3
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of the prior art is that after the single-pot reaction, it needs to be cleaned and re-feeding, which greatly reduces the reaction efficiency, and multiple types of reactions occur in the single-pot, which requires high technical requirements for the reactor. Moreover, it is difficult to Realize the motorized adjustment of the relative output of HEDP and acetyl chloride. In addition, the aqueous acetic acid produced by hydrolysis in the later stage cannot be directly used, which increases the difficulty of recovering acetic acid.

Method used

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  • Production method and system for co-production of acetyl chloride by 1-hydroxyethylidene-1,1-diphosphonicacid
  • Production method and system for co-production of acetyl chloride by 1-hydroxyethylidene-1,1-diphosphonicacid

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Effect test

Embodiment 1

[0031] A kind of production method of hydroxyethylene diphosphoric acid co-production acetyl chloride is carried out with the following process steps:

[0032] (1) Under normal pressure, start the reactor 1 to stir, put the phosphorus trichloride B stored in the storage tank into 2400kg in the phosphorus trichloride head tank, and pump 3150kg of acetic acid A stored in the storage tank into the reaction Kettle 1, control the speed of 310L / h, and start to drop phosphorus trichloride B into the reaction kettle at the same time, control the speed of 160L / h, and the temperature in the reaction kettle 1 is less than 45°C;

[0033] (2) The mixed material is preheated by the two-stage heat exchanger 4, the temperature of the first-stage heat exchanger 4-1 is 70°C, the heat source comes from waste heat recovery, the temperature of the second-stage heat exchanger 4-2 is 100°C, and the heat source comes from the boiler 8 steam;

[0034] (3) After the material is preheated, it enters th...

Embodiment 2

[0038] A kind of production method of hydroxyethylene diphosphoric acid co-production acetyl chloride is carried out with the following process steps:

[0039] (1) Under normal pressure, start the reactor 1 to stir, put the phosphorus trichloride B stored in the storage tank into 2200kg in the phosphorus trichloride head tank, and pump 3000kg of acetic acid A stored in the storage tank into the reaction Kettle 1, control the speed of 290L / h, and start to drop phosphorus trichloride B into the reaction kettle at the same time, control the speed of 150L / h, and the temperature in the reaction kettle 1 is less than 45°C;

[0040] (2) The mixed material is preheated by the two-stage heat exchanger 4, the temperature of the first-stage heat exchanger 4-1 is 80°C, the heat source comes from waste heat recovery, the temperature of the second-stage heat exchanger 4-2 is 105°C, and the heat source comes from the boiler 8 steam;

[0041] (3) After the material is preheated, it enters th...

Embodiment 3

[0045] A kind of production method of hydroxyethylene diphosphoric acid co-production acetyl chloride is carried out with the following process steps:

[0046] (1) Under normal pressure, start the reactor 1 to stir, put the phosphorus trichloride B stored in the storage tank into 2500kg in the phosphorus trichloride head tank, and pump 3300kg of acetic acid A stored in the storage tank into the reaction Kettle 1, control the speed of 320L / h, and at the same time start to drop phosphorus trichloride B into the reaction kettle, control the speed of 180L / h, and the temperature in the reaction kettle 1 is less than 45°C;

[0047] (2) The mixed material is preheated by the two-stage heat exchanger 4, the temperature of the first-stage heat exchanger 4-1 is 65°C, the heat source comes from waste heat recovery, the temperature of the second-stage heat exchanger 4-2 is 95°C, and the heat source comes from the boiler 8 steam;

[0048] (3) After the material is preheated, it enters the...

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Abstract

The invention provides a production method for co-production of acetyl chloride by 1-hydroxyethylidene-1,1-diphosphonicacid. The method comprises the following steps: starting a reaction still for stirring, pumping a certain amount of acetic acid or acetic acid aqueous solution in, and meanwhile dripping a certain amount of phosphorus trichloride into the reaction still for mixing; after mixing, leading into a heat exchanger for preheating; preheating a mixed material, leading into a synthesis reactor for an esterification reaction, enabling generated acetyl chloride to enter into a rectifying tower to be separated to obtain high-purity acetyl chloride or back drop into the synthesis reactor, enabling hydrochloric acid and uncondensed acetyl chloride to enter a multi-stage exhaust absorption apparatus; enabling generated acetic ester to enter a hydrolysis kettle for hydrolyzation, promoting acetic ester to evaporate out by negative pressure operation to be reused, replenishing deionized water to promote the hydrolyzation to obtain HEDP, and reusing excess heat through a steam recycling machine on the heat exchanger. The production method has the following beneficial effects: the production efficiency is promoted; the operative difficulty and labor intensity are reduced; the technical parameter requirements on the synthesis reactor can be lowered; the reaction efficiency can be greatly improved; product overstocking caused by acetyl chloride encountering poor sales is avoided; the production cost is saved; the exhaust emission is reduced.

Description

technical field [0001] The invention belongs to the technical field of chemical production, and in particular relates to a production method and system for co-producing acetyl chloride from hydroxyethylene diphosphate. Background technique [0002] Hydroxyethylene diphosphate, referred to as HEDP, structural formula: (H 2 PO 3 ) 2 C(OH)CH 3 . The pure product is a white crystal, easily soluble in water and methanol, with a melting point of 198-199°C. HEDP can form stable complexes with various metal ions such as iron, copper, zinc, etc., can dissolve oxides on the metal surface, and is still stable at high pH values. It is usually used as a complexing agent, water quality stabilizer, and masking agent , extractant, etc. HEDP can form six-ring chelates with metal ions in water, especially calcium ions, so it has good scale inhibition effect and obvious solubility limit effect. When used in combination with other water treatment agents, it shows ideal synergy Effect, wi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07F9/38C07C51/60C07C51/64C07C53/40
CPCC07F9/386C07C51/60C07C51/64C07C53/40
Inventor 李光海王成彩刘康王宏义
Owner 天津科维津宏环保科技有限公司
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