CN202410472U - Tail gas treatment device for production of diallyl phthalate - Google Patents

Tail gas treatment device for production of diallyl phthalate Download PDF

Info

Publication number
CN202410472U
CN202410472U CN201220020761XU CN201220020761U CN202410472U CN 202410472 U CN202410472 U CN 202410472U CN 201220020761X U CN201220020761X U CN 201220020761XU CN 201220020761 U CN201220020761 U CN 201220020761U CN 202410472 U CN202410472 U CN 202410472U
Authority
CN
China
Prior art keywords
condenser
tail gas
diallyl phthalate
utility
model
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
CN201220020761XU
Other languages
Chinese (zh)
Inventor
李庆山
张光
钟同涛
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.)
SHOUGUANG NUOMENG CHEMICAL CO Ltd
Original Assignee
SHOUGUANG NUOMENG 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 SHOUGUANG NUOMENG CHEMICAL CO Ltd filed Critical SHOUGUANG NUOMENG CHEMICAL CO Ltd
Priority to CN201220020761XU priority Critical patent/CN202410472U/en
Application granted granted Critical
Publication of CN202410472U publication Critical patent/CN202410472U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The utility model relates to a tail gas treatment device for production of diallyl phthalate. The device comprises a vacuum pump and a condenser, wherein the air inlet end of the vacuum pump is connected with the tail gas hole of a diallyl phthalate synthesis kettle; the condenser is arranged at the air outlet end of the vacuum pump; and the condenser is connected with a recovery groove for receiving a feed liquid. The device disclosed by the utility model can condense and recover allyl alcohol in the tail gas, so that environment pollution is avoided, the waste of raw materials is reduced, and production cost is reduced.

Description

Be used for the exhaust gas processing device that diallyl phthalate is produced
Technical field
The utility model relates to a kind of chemical industry equipment, is specifically related to a kind of exhaust gas processing device that diallyl phthalate is produced that is used for.
Background technology
Diallyl phthalate can prepare the DAP plastics, and these plastics are the excellent thermosetting plasticses of a kind of electric property, and its characteristics: electrical property is excellent, and under the condition of high temperature, changes less; During moulding mobile better, be prone to make complex-shaped small-sized and have a making of tiny inserts; Dimensional stability is good; To the metal insert non-corrosiveness.Therefore the DAP plastics are to make electrical equipment and the indispensable a kind of material of electronic component, and diallyl phthalate has crucial status especially.
The general production method that adopts of diallyl phthalate is: phthalic anhydride generates the phthalic acid sodium salt with the liquid caustic soda reaction, again with propenyl esterification and get bullion under 40-60 ℃, negative pressure.
In actual production process, better carry out in order to make reaction, be negative pressure in the synthesis reactor of general diallyl phthalate; Need utilize vavuum pump that the gas in the agitated reactor is extracted out; And the producing equipment of the diallyl phthalate of traditional structure all directly is discharged into the gas of extracting out in the atmosphere, has not only polluted environment, and can contain raw material propylene alcohol in the gas of discharging; The significant wastage that this will cause raw material causes production cost to improve.
The utility model content
The utility model technical problem to be solved provides and is used for the exhaust gas processing device that diallyl phthalate is produced, and it can effectively reclaim the useful material in the tail gas, reduces production costs, thereby eliminates defective in the above-mentioned background technology.
For solving the problems of the technologies described above, the technical scheme of the utility model is:
Be used for the exhaust gas processing device that diallyl phthalate is produced; It is characterized in that; Comprise vavuum pump and condenser; The inlet end of said vavuum pump is connected in the tail gas mouth of diallyl phthalate synthesis reactor, and said condenser is arranged at the outlet side of said vavuum pump, and said condenser is connected with the accumulator tank that is used to receive feed liquid.
As a kind of improvement, be provided with cooling coil in the said condenser, feed condensed water in the said cooling coil.This condenser structure is simple, and condensation effect is good, can with the useful material of the overwhelming majority in the tail gas for example propenyl be condensed into liquid phase, and hold back.
As a kind of improvement, said vavuum pump comprises screw pump, and screw pump can produce stronger negative pressure, is beneficial to the carrying out of reaction, also is beneficial to separate impurities in the product.
The utility model is when work, and screw pump starts, can be with the inner negative pressure that produces of synthesis reactor; Synthesis reactor tail gas mouth then can be discharged tail gas, contains for example propenyl of many useful materials in the tail gas, and tail gas can at first get into condenser; Cooling coil in the condenser can cool to tail gas, and at this moment, the propenyl that contains in the tail gas can become liquid phase and be trapped; The propenyl of liquid phase gets into accumulator tank, utilizes again after can passing through purification process.
Owing to adopted technique scheme, the beneficial effect of the utility model is:
The exhaust gas processing device that the utility model provides is applicable to the production process of diallyl phthalate, and it is connected with vavuum pump and condenser in order at the tail gas mouth of synthesis reactor; Based on this structure; Tail gas can at first get into condenser, and the cooling coil in the condenser can cool to tail gas, and the propenyl that contains in the tail gas can become liquid phase and be trapped; The propenyl of liquid phase gets into accumulator tank, utilizes again after the purification process; Not only avoid environmental pollution, and reclaimed raw material, reduced production cost.
The utility model is the condenser that set inside has cooling coil, and this condenser structure is simple, and condensation effect is good, can with the useful material of the overwhelming majority in the tail gas for example propenyl be condensed into liquid phase, and hold back.
The utility model uses screw pump, and screw pump can produce stronger negative pressure, is beneficial to the carrying out of reaction, also is beneficial to separate impurities in the product.
Description of drawings
Accompanying drawing is the utility model structural representation;
Among the figure: 1. vavuum pump, 2. condenser, 3. synthesis reactor, 4. tail gas mouth, 5. accumulator tank, 6. cooling coil.
The specific embodiment
For technological means, creation characteristic that the utility model is realized, reach purpose and be easy to understand understanding with effect, below in conjunction with concrete diagram, further set forth the utility model.
Shown in accompanying drawing; Be used for the exhaust gas processing device that diallyl phthalate is produced; Comprise vavuum pump 1 and condenser 2; The inlet end of said vavuum pump 1 is connected in the tail gas mouth 4 of diallyl phthalate synthesis reactor 3, and said condenser 2 is arranged at the outlet side of said vavuum pump 1, and said condenser 2 is connected with the accumulator tank 5 that is used to receive feed liquid.
In the present embodiment, be provided with cooling coil 6 in the said condenser 2, feed condensed water in the said cooling coil 6.This condenser 2 is simple in structure, and condensation effect is good, can with the useful material of the overwhelming majority in the tail gas for example propenyl be condensed into liquid phase and hold back.
Simultaneously, said vavuum pump 1 adopts screw pump, and screw pump can produce stronger negative pressure, is beneficial to the carrying out of reaction, also is beneficial to separate impurities in the product.
Describe the course of work of the utility model in detail below in conjunction with accompanying drawing.
The utility model is when work, and vavuum pump 1 starts, and can make the synthesis reactor 3 inner negative pressure that produce; 4 in the tail gas mouth of synthesis reactor 3 can be discharged tail gas, and tail gas can at first get into condenser 2, and the cooling coil 6 in the condenser 2 can cool to tail gas; At this moment; The propenyl that contains in the tail gas can become liquid phase and be trapped, and the propenyl of liquid phase gets into accumulator tank 5, utilizes again after can passing through purification process.
The utility model is not limited to the above-mentioned specific embodiment, and all are based on the technical conceive of the utility model, and the structural improvement of having done all falls among the protection domain of the utility model.

Claims (3)

1. be used for the exhaust gas processing device that diallyl phthalate is produced; It is characterized in that: comprise vavuum pump and condenser; The inlet end of said vavuum pump is connected in the tail gas mouth of diallyl phthalate synthesis reactor; Said condenser is arranged at the outlet side of said vavuum pump, and said condenser is connected with the accumulator tank that is used to receive feed liquid.
2. the exhaust gas processing device that is used for diallyl phthalate production as claimed in claim 1 is characterized in that: be provided with cooling coil in the said condenser.
3. the exhaust gas processing device that is used for diallyl phthalate production as claimed in claim 1, it is characterized in that: said vavuum pump comprises screw pump.
CN201220020761XU 2012-01-17 2012-01-17 Tail gas treatment device for production of diallyl phthalate Expired - Fee Related CN202410472U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201220020761XU CN202410472U (en) 2012-01-17 2012-01-17 Tail gas treatment device for production of diallyl phthalate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201220020761XU CN202410472U (en) 2012-01-17 2012-01-17 Tail gas treatment device for production of diallyl phthalate

Publications (1)

Publication Number Publication Date
CN202410472U true CN202410472U (en) 2012-09-05

Family

ID=46735271

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201220020761XU Expired - Fee Related CN202410472U (en) 2012-01-17 2012-01-17 Tail gas treatment device for production of diallyl phthalate

Country Status (1)

Country Link
CN (1) CN202410472U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103446842A (en) * 2013-08-30 2013-12-18 张家港市三联化工科技有限公司 Tail gas treatment device for MAQ-ME (R-(+)-2-(4-Hydroxyphenoxy) drying
CN104826353A (en) * 2015-04-28 2015-08-12 广州市海同机电设备有限公司 Solvent recovery system and technology thereof
CN105032111A (en) * 2014-11-26 2015-11-11 安徽嘉智信诺化工有限公司 Condensation recycling device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103446842A (en) * 2013-08-30 2013-12-18 张家港市三联化工科技有限公司 Tail gas treatment device for MAQ-ME (R-(+)-2-(4-Hydroxyphenoxy) drying
CN103446842B (en) * 2013-08-30 2016-01-20 张家港市三联化工科技有限公司 For the exhaust gas processing device of MAQ-ME drying
CN105032111A (en) * 2014-11-26 2015-11-11 安徽嘉智信诺化工有限公司 Condensation recycling device
CN105032111B (en) * 2014-11-26 2018-03-02 安徽嘉智信诺化工股份有限公司 A kind of condensate recycling device
CN104826353A (en) * 2015-04-28 2015-08-12 广州市海同机电设备有限公司 Solvent recovery system and technology thereof

Similar Documents

Publication Publication Date Title
CN109650415B (en) Method for extracting lithium carbonate from scrapped lithium iron phosphate battery positive electrode powder
CN107017444A (en) A kind of method of metal recovery in waste lithium iron phosphate battery
CN105789726A (en) Method for preparing nickel-cobalt-manganese ternary material precursor from waste lithium ion battery
CN202410472U (en) Tail gas treatment device for production of diallyl phthalate
CN104183887A (en) Green method for dismantling, separation and recovery of waste LiCoO2 battery
CN103451673B (en) The production method of electrolytic metal Mn
CN104858447A (en) Preparation method and equipment for high-conductivity nano silver for PCB
CN202141345U (en) Tail gas recovering system for annealing furnace
CN103199319A (en) Method for recycling lithium cobalt oxide from waste positive electrode of lithium cobalt oxide battery
CN204400883U (en) Pentamethylene diamine purification system
CN205109056U (en) Sour vapor removal recovery unit of red fuming nitric acid (RFNA) production
CN101629250A (en) Method for reclaiming soluble manganese from electrolytic metal manganese filter-press residues
CN102874848A (en) Method for recovering sodium bicarbonate and organic acid sodium salt from cyclohexanone waste alkali solution
CN111170359A (en) Device and process for preparing red lead from desulfurized lead
CN109193061A (en) A kind of lithium battery recovery process
CN204768117U (en) Organic solvent recovery unit among wet article dry run of diphenyl sulphone (DPS)
CN204639140U (en) A kind of equipment preparing PCB high connductivity Nano Silver
CN103588266A (en) Chemical recycling method for treating organic acid in wastewater from electrode foil chemical synthesis
CN203235409U (en) Device for collecting and treating waste gas in fluorescent powder waste treatment process
CN202410638U (en) Transfer pot for producing diallyl phthalate
CN202865198U (en) Polyethylene glycol filtering and purifying device
CN102787247A (en) Method for regenerating aluminium-copper intermediate alloy by extruding waste copper-clad aluminium conductor and waste copper conductor for three times
CN102515253B (en) Production method for producing zinc oxide by ammonia process and comprehensively utilizing waste water
CN101786937B (en) Chlorinated paraffin vacuum removal process and equipment
CN101880773A (en) Manufacturing process for producing synthetic reducing agent by using waste slag of electrolytic manganese and application of synthetic reducing agent

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: 20120905

Termination date: 20150117

EXPY Termination of patent right or utility model