CN203370441U - Improved HCL (Hydrogen Chloride) tail gas absorption device - Google Patents

Improved HCL (Hydrogen Chloride) tail gas absorption device Download PDF

Info

Publication number
CN203370441U
CN203370441U CN201320297759.1U CN201320297759U CN203370441U CN 203370441 U CN203370441 U CN 203370441U CN 201320297759 U CN201320297759 U CN 201320297759U CN 203370441 U CN203370441 U CN 203370441U
Authority
CN
China
Prior art keywords
hcl
absorption tower
tail gas
improved
glycerol
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201320297759.1U
Other languages
Chinese (zh)
Inventor
林锦堂
吴锦杰
孙艺亮
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
FUJIAN HAOBANG CHEMICAL Co Ltd
Original Assignee
FUJIAN HAOBANG CHEMICAL Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by FUJIAN HAOBANG CHEMICAL Co Ltd filed Critical FUJIAN HAOBANG CHEMICAL Co Ltd
Priority to CN201320297759.1U priority Critical patent/CN203370441U/en
Application granted granted Critical
Publication of CN203370441U publication Critical patent/CN203370441U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The utility model provides an improved HCL (Hydrogen Chloride) tail gas absorption device. The improved HCL tail gas absorption device is composed of a mixer, a glycerol absorption tower and a reaction kettle, wherein the mixer is connected with the upper end of the glycerol absorption tower by an input pipeline; the reaction kettle is connected with the bottom end of the glycerol absorption tower by an output pipeline; the reaction kettle is further connected with an HCL conveying pipeline and an overflowing opening; the bottom end of the glycerol absorption tower is further connected with a reflowing pipeline and the top of the glycerol absorption tower is connected with the output pipeline. According to the improved HCL tail gas absorption device, the flow of the glycerol absorption tower is simple, the discharging amount of waste acid water is reduced greatly, the HCL utilization rate is improved and the energy consumption is reduced.

Description

Improved HCL device for absorbing tail gas
Technical field
The utility model belongs to the chemical industry equipment field, and what be specifically related to is a kind of improved HCL device for absorbing tail gas.
Background technology
at present, in the process of producing at epoxychloropropane, be entrained with organic components in HCL tail gas due to discharge, the absorption plant utilized at present is to adopt clear water absorption tower device, the concentrated acid produced after absorbing with clear water can not enter salt adding and resolve, and can only pass through the alkali neutralisation treatment, thereby cause the waste of alkali resource, reduced the HCL utilization rate, making to prepare the epoxychloropropane production cost increases greatly.
Summary of the invention
The purpose of this utility model is for the deficiencies in the prior art, and a kind of improved HCL device for absorbing tail gas greatly reduced production costs is provided.
The utility model is achieved through the following technical solutions: improved HCL device for absorbing tail gas, by blender, glycerine absorption tower and reactor, formed, described blender is connected with the upper end on glycerine absorption tower by input channel, and reactor is connected with the bottom on glycerine absorption tower by output channel.
Also be connected with HCL conveyance conduit and overfall on described reactor.
The bottom on described glycerine absorption tower also is connected with reflux line, and top is connected with output channel.
The beneficial effects of the utility model embody and are: compared with prior art, the utility model tail gas absorber flow process is simple, greatly reduces the discharge capacity of waste acid water, has improved the HCL utilization rate, has reduced energy consumption.
The accompanying drawing explanation
Below in conjunction with accompanying drawing, the utility model is described in detail.
Fig. 1 is the utility model structural representation.
Following is the concrete title of each sign in figure: 1 blender, 2 conveyance conduits, 3 output channels, 4 glycerine absorption towers, 5 HCL conveyance conduits, 6 reflux lines, 7 reactors, 8 input channels, 9 output channels.
The specific embodiment
As shown in Figure 1, improved HCL device for absorbing tail gas, blender 1, glycerine absorption tower 4 and reactor 7, consist of, described blender 1 is connected with the upper end on glycerine absorption tower 4 by input channel 8, and reactor 7 is connected with the bottom on glycerine absorption tower 4 by output channel 9.
Also be connected with HCL conveyance conduit 5 and overfall on described reactor 7.
The bottom on described glycerine absorption tower 4 also is connected with reflux line 6, and top is connected with output channel 3.
The utility model workflow is: after the glycerine outside battery limit (BL) and acetic acid are delivered to that blender 1 is interior and mixed by pump by a certain percentage, enter into glycerine absorption tower 4, mixture absorbs column bottoms pump by glycerine continuously and is transported in reactor 7, and pass into HCL in reactor 7 simultaneously, control material and reacted under suitable temperature and pressure, unnecessary HCL enters in the glycerine absorption tower and absorbs recycling.

Claims (3)

1. improved HCL device for absorbing tail gas, it is characterized in that: blender, glycerine absorption tower and reactor, consist of, blender is connected with the upper end on glycerine absorption tower by input channel, and reactor is connected with the bottom on glycerine absorption tower by output channel.
2. improved HCL device for absorbing tail gas according to claim 1, is characterized in that: also be connected with HCL conveyance conduit and overfall on reactor.
3. improved HCL device for absorbing tail gas according to claim 1, it is characterized in that: the bottom on glycerine absorption tower also is connected with reflux line, and top is connected with output channel.
CN201320297759.1U 2013-05-28 2013-05-28 Improved HCL (Hydrogen Chloride) tail gas absorption device Expired - Fee Related CN203370441U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320297759.1U CN203370441U (en) 2013-05-28 2013-05-28 Improved HCL (Hydrogen Chloride) tail gas absorption device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320297759.1U CN203370441U (en) 2013-05-28 2013-05-28 Improved HCL (Hydrogen Chloride) tail gas absorption device

Publications (1)

Publication Number Publication Date
CN203370441U true CN203370441U (en) 2014-01-01

Family

ID=49832998

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320297759.1U Expired - Fee Related CN203370441U (en) 2013-05-28 2013-05-28 Improved HCL (Hydrogen Chloride) tail gas absorption device

Country Status (1)

Country Link
CN (1) CN203370441U (en)

Similar Documents

Publication Publication Date Title
CN104138703B (en) Between/paraphthaloyl chloride produce in waste gas treatment process and device
CN203754482U (en) Wet-type oxidation treatment device of waste water
CN201735309U (en) Unitization efficient tail gas absorbing device for leather tail gas treatment
CN201593028U (en) Device used in benzyl alcohol continuous hydrolysis technique
CN203370441U (en) Improved HCL (Hydrogen Chloride) tail gas absorption device
CN201990481U (en) Concentration device for dilute hydrochloric acid
CN203990257U (en) Between/paraphthaloyl chloride produce in emission-control equipment
CN203461829U (en) Device for recycling waste ammonia gas of LED (Light-Emitting Diode) gallium nitride production furnace as saturated ammonia water
CN203017976U (en) Concentrated nitric acid mist recycling device
CN202131245U (en) Equipment for recycling bromotrifluoromethane
CN202606053U (en) Totally-closed static pipeline continuous precipitation system for rear earth precipitation and transformation
CN203346371U (en) Sludge resource utilization device
CN204125192U (en) The useless time sodium recycle device of acetylene
CN204058292U (en) A kind of phosphorus ammonium sludge produces nitro-compound fertilizer device
CN202063741U (en) Calcium nitrate solution reacting and producing device
CN203820663U (en) Production system of 2-chlorine-4-nitrotoluene
CN204356141U (en) For the anaerobic reaction device of changing food waste process
CN203212480U (en) Special equipment for slow and controlled release fertilizer by using urea sulfate and urea formaldehyde co-production process
CN202729807U (en) Circular-flowing type energy-saving neutral reactor in ammonium phosphate systematic production
CN202164140U (en) Concentrated water recycling device
CN203316112U (en) Acid mist emission control device of reaction kettle
CN203212482U (en) Reactor for novel urea formaldehyde humic acid organic ecological fertilizer
CN203342799U (en) Pressure-relief buffer tank applied to hydantoin production equipment
CN202161907U (en) Exhaust emission device for trimethyl orthoformate and triethyl orthoformate amination and alcoholysis procedures
CN202263414U (en) Tail gas recovery device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140101

Termination date: 20190528

CF01 Termination of patent right due to non-payment of annual fee