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Preparation device and preparation method for high-purity hydrochloric acid production by monochlorodifluoromethane byproduct HCL

A technology of difluorochloromethane and high-purity hydrochloric acid, which is applied in the preparation of halogenated hydrocarbons, preparation of halogen substitution, purification of chlorine/hydrogen chloride, etc., can solve problems such as high impurity content, non-environmental protection, and low added value of 31% hydrochloric acid , to prevent secondary pollution and reduce waste

Pending Publication Date: 2016-08-17
江苏梅兰化工有限公司
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Problems solved by technology

[0002] The production of chlorodifluoromethane is based on chloroform and HF as raw materials. The two react in a fluorination reactor according to a certain ratio to form chlorodifluoromethane. The by-product is HCL, which is separated at the top of the tower through high-pressure and low-temperature rectification. Produce HCL, which contains 100-200PPm of HF, about 1.5% of F23, about 0.2% of F22, and 70-100PPm of free chlorine. The traditional process uses AL2O3 to absorb HF and then absorbs it with water to produce 31% hydrochloric acid because of its high impurity content. , the production of 31% hydrochloric acid has low added value and does not meet the requirements of environmental protection

Method used

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  • Preparation device and preparation method for high-purity hydrochloric acid production by monochlorodifluoromethane byproduct HCL

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Embodiment Construction

[0010] The invention discloses a preparation method for producing high-purity hydrochloric acid by using HCL as a by-product of difluorochloromethane. Containing HF100-200PPm, about 1.5% of F23, about 0.2% of F22, 70-100PPm of free chlorine, the storage tank 1 of HCL enters the primary falling film absorber 4 after passing through the HCL regulating valve 2 and the HCL flow meter 3 At the inlet, the soft water tank 5 enters the upper part of the washing tower after passing through the soft water flow meter 6 and the soft water regulating valve 7, and the HCL flow is connected with the soft water flow for ratio adjustment. The 31% hydrochloric acid generated after the membrane absorber 10 is stored and connected to the middle tank I11 and the middle tank II12. The volume of the middle tank I11 and the middle tank II12 is large enough to store the output for one day. The condensed gas is sent to incineration through the water washing tower 8, the alkali washing tower 17, and the...

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Abstract

The invention discloses a preparation method for high-purity hydrochloric acid production by monochlorodifluoromethane byproduct HCL. The preparation method includes: producing 31% hydrochloric acid; enabling the 31% hydrochloric acid in an intermediate tank I (11) and an intermediate tank II (12) to cyclically adsorb fluorine ions, free chlorine and organics through a circulating pump (13), an adsorption bed I (14) and an adsorption bed II (15); after sampling analysis is qualified, sending to a finished product tank (16) of 31% high-purity hydrochloric acid. The invention further discloses a preparation device for high-purity hydrochloric acid production by the monochlorodifluoromethane byproduct HCL. The preparation device is characterized by comprising a water washing tower (8), a primary falling film absorber (9), a secondary falling film absorber (10), an alkaline tower (17), the intermediate tank I (11), the intermediate tank II (12), the adsorption bed I (14) and the adsorption bed II (15).

Description

technical field [0001] The invention relates to a preparation method and a preparation device for producing high-purity hydrochloric acid by using HCL as a by-product of difluorochloromethane. Background technique [0002] The production of chlorodifluoromethane is based on chloroform and HF as raw materials. The two react in a fluorination reactor according to a certain ratio to form chlorodifluoromethane. The by-product is HCL, which is separated at the top of the tower through high-pressure and low-temperature rectification. Produce HCL, which contains 100-200PPm of HF, about 1.5% of F23, about 0.2% of F22, and 70-100PPm of free chlorine. The traditional process uses AL2O3 to absorb HF and then absorbs it with water to produce 31% hydrochloric acid because of its high impurity content. , the production of 31% hydrochloric acid has low added value and does not meet the requirements of environmental protection. Contents of the invention [0003] The invention provides a ...

Claims

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Application Information

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IPC IPC(8): C07C19/10C07C17/20C01B7/07
CPCC01B7/0718C07C17/206C07C19/10
Inventor 王卫国
Owner 江苏梅兰化工有限公司
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