CN202191720U - Recovery device for tail gas of oxirane for polyether polyol - Google Patents

Recovery device for tail gas of oxirane for polyether polyol Download PDF

Info

Publication number
CN202191720U
CN202191720U CN2011203386301U CN201120338630U CN202191720U CN 202191720 U CN202191720 U CN 202191720U CN 2011203386301 U CN2011203386301 U CN 2011203386301U CN 201120338630 U CN201120338630 U CN 201120338630U CN 202191720 U CN202191720 U CN 202191720U
Authority
CN
China
Prior art keywords
tail gas
oxirane
condenser
retracting device
collecting tank
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
CN2011203386301U
Other languages
Chinese (zh)
Inventor
金大映
程华艺
冯凤
陈伴生
赵弘哲
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.)
Leah Polyol (nanjing) Co Ltd
Original Assignee
Leah Polyol (nanjing) 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 Leah Polyol (nanjing) Co Ltd filed Critical Leah Polyol (nanjing) Co Ltd
Priority to CN2011203386301U priority Critical patent/CN202191720U/en
Application granted granted Critical
Publication of CN202191720U publication Critical patent/CN202191720U/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 discloses a recovery device for tail gas of oxirane for polyether polyol, which is particularly applicable to a storage tank for oxirane, a raw material of the polyether polyol. The recovery device comprises a condenser, a collection tank and a tail gas absorber, wherein the condenser is connected with a tail gas outlet of the storage tank for the oxirane; the outlet of the condenser is connected with the collection tank; and a gas outlet at the upper part of the collection tank is connected with the tail gas absorber. After being cooled by the condenser, the tail gas of the oxirane flows back into the collection tank, and is fed into the storage tank for the oxirane by a reflux pump at the bottom of the collection tank; and noncondensable gas is absorbed by the tail gas absorber and then directly discharged. The device can recover the tail gas in the storage process of the oxirane, greatly reduces the loss of the oxirane in the storage process and improves the safety in the storage process. The device is simple in structure and has practical application value in the production process.

Description

The retracting device of polyether polyol reaction dissolvent oxirane tail gas
Technical field
The utility model relates to a cover chemical industry equipment, is specifically related to a kind of retracting device of polyether polyol reaction dissolvent oxirane tail gas, and this equipment is particularly useful for the recovery of oxirane storage tank tail gas.
Background technology
Use reaction dissolvent oxirane during polyether polyol is produced, the boiling point of oxirane is 10.4 ℃, and flash-point belongs to A-grade in the first class's class hazardous chemical less than-17.8 ℃, and it stores high requirement.The storing mode that present most at home producer uses stores as the pressure pot type; The drawback of the maximum of this storage is that storage process can discharge a large amount of tail gas; The tail gas that volatilizes has not only increased the proportion of goods damageds of the raw material that stores, and also increases simultaneously the danger coefficient of storage process greatly.External storing mode has adopted the storing mode of freezing type at present; Reduced the loss in the storage process; But the problem that the freezing type storage exists tail gas to absorb too, the utility model just is being based on above defective, and the oxirane storage device is improved; Guarantee that the loss of storing minimizes, and guarantee the security performance of storage.
Summary of the invention
The purpose of the utility model is to provide a kind of retracting device of polyether polyol reaction dissolvent oxirane tail gas; This device can reclaim the tail gas in the oxirane storage process; Greatly reduce the loss of the oxirane in the storage process, improve the security in the storage process.
The utility model is realized through following technical scheme:
A kind of retracting device of polyether polyol reaction dissolvent oxirane tail gas; It is characterized in that: described retracting device comprises condenser, collecting tank and tail gas absorber; Condenser is connected with the outlet of oxirane storage tank tail gas; Condensator outlet connects collecting tank, and the outlet of collecting tank upper gas connects tail gas absorber.
Chilled brine below the described condenser outer circulation-10 ℃.
Described retracting device also comprises the pipeline that is connected between collecting tank and the oxirane storage tank, and pipeline is provided with the recovery pump.Reclaim pump and use explosion-proof pump.
The condensed oxirane solvent of described collecting tank collecting ring oxidative ethane tail gas; Tail gas absorber adopts the water absorption tower usually, is used for absorbing the fixed gas in the oxirane tail gas.The height of tail gas absorber must be higher than 15 meters, so that exhaust emissions reaches environmental protection standard.
Utilize the retracting device of the utility model, its oxirane tail gas recycle process is following:
1) opens-10 ℃ of chilled waters of condenser, cool off through the condenser outer circulation.
2) open breather valve and the safety valve bottom valve that connecting ring oxidative ethane storage tank tail gas exports, oxirane storage tank tail gas is through condenser condenses.
3) the tail gas condensate liquid gets into collecting tank, and interior circulation insulation is opened.
4) when the collecting tank liquid level reaches 80%, open the recovery pump, directly pump into the oxirane storage tank.
5) fixed gas directly discharges in the atmosphere after tail gas absorber water absorbs.
The retracting device of the polyether polyol reaction dissolvent oxirane tail gas of the utility model carries out condensation to oxirane tail gas and handles with absorbing, and with being reclaimed by collecting tank after the condensation of oxirane tail gas, fixed gas absorbs the back discharging by the absorption tower.This device can reclaim the tail gas in the oxirane storage process, greatly reduces the loss of the oxirane in the storage process, improves the security in the storage process simultaneously.The utility model apparatus structure is simple, has the value of practical application aborning.
Below in conjunction with accompanying drawing the utility model is described in detail.The protection domain of the utility model does not exceed with the specific embodiment, but is limited claim.
Description of drawings
The structural representation of the oxirane device for recovering tail gas of Fig. 1 the utility model.
Wherein: 1, oxirane storage tank, 2, condenser, 3, collecting tank, 4, tail gas absorber, 5, reclaim pump.
The specific embodiment
Referring to shown in Figure 1, a kind of retracting device of polyether polyol reaction dissolvent oxirane tail gas comprises condenser 2, collecting tank 3, tail gas absorber 4 and reclaims pump 5.
The condenser 2 of said device is connected with the tail gas outlet of oxirane storage tank 1, and condenser 2 outer circulations-10 ℃ chilled water cools off oxirane tail gas.
Condenser 2 outlets connect collecting tank 3, and the outlet of collecting tank 3 upper gas connects tail gas absorber 4.After the condensation of oxirane tail gas, wherein the oxirane solvent gets in the collecting tank 3, and fixed gas gets into tail gas absorber 4 by the outlet of collecting tank 3 upper gas.Tail gas absorber is the water absorption tower, highly is higher than 15 meters, makes exhaust emissions reach environmental protection standard.
Between collecting tank 3 and oxirane storage tank 1, be connected by pipeline, pipeline is provided with and reclaims pump 5.Reclaim pump 5 and use explosion-proof pump.When collecting tank 3 liquid levels reach 80%, the oxirane that reclaims is directly pumped in the oxirane storage tank 1 by reclaiming pump 5.
Utilize the above-mentioned retracting device of the utility model, its oxirane tail gas recycle process is following:
1) opens-10 ℃ of chilled waters of condenser 2, cool off through condenser 2 outer circulations.
2) open breather valve and the safety valve bottom valve that connecting ring oxidative ethane storage tank 1 tail gas exports, oxirane storage tank 1 tail gas is through condenser 2 condensations.
3) the tail gas condensate liquid gets into collecting tank 3, and interior circulation insulation is opened.
4) when collecting tank 3 liquid levels reach 80%, open and reclaim pump 5, directly pump into oxirane storage tank 1.
5) fixed gas directly discharges in the atmosphere after tail gas absorber 4 water absorb.

Claims (5)

1. the retracting device of a polyether polyol reaction dissolvent oxirane tail gas; It is characterized in that: described retracting device comprises condenser (2), collecting tank (3) and tail gas absorber (4); Condenser (2) is connected with the outlet of oxirane storage tank (1) tail gas; Condenser (2) outlet connects collecting tank (3), and the outlet of collecting tank (3) upper gas connects tail gas absorber (4).
2. the retracting device of oxirane tail gas according to claim 1 is characterized in that: chilled brine below condenser (2) outer circulation-10 ℃.
3. the retracting device of oxirane tail gas according to claim 1 is characterized in that: pipeline is connected between described collecting tank (3) and the oxirane storage tank (1), and pipeline is provided with and reclaims pump (5).
4. the retracting device of oxirane tail gas according to claim 3 is characterized in that: described recovery pump (5) is explosion-proof pump.
5. the retracting device of oxirane tail gas according to claim 1 is characterized in that: described tail gas absorber (4) is the water absorption tower, and height is greater than 15 meters.
CN2011203386301U 2011-09-09 2011-09-09 Recovery device for tail gas of oxirane for polyether polyol Expired - Fee Related CN202191720U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011203386301U CN202191720U (en) 2011-09-09 2011-09-09 Recovery device for tail gas of oxirane for polyether polyol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011203386301U CN202191720U (en) 2011-09-09 2011-09-09 Recovery device for tail gas of oxirane for polyether polyol

Publications (1)

Publication Number Publication Date
CN202191720U true CN202191720U (en) 2012-04-18

Family

ID=45946652

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011203386301U Expired - Fee Related CN202191720U (en) 2011-09-09 2011-09-09 Recovery device for tail gas of oxirane for polyether polyol

Country Status (1)

Country Link
CN (1) CN202191720U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108358151A (en) * 2018-04-23 2018-08-03 中国化学赛鼎宁波工程有限公司 A kind of factory monitors with ethylene oxide, storage, recycling and handling system
PL425052A1 (en) * 2018-03-28 2019-10-07 Icso Chemical Production Spółka Z Ograniczoną Odpowiedzialnością Method for reduction of emission of volatile organic compounds and the system for its execution

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL425052A1 (en) * 2018-03-28 2019-10-07 Icso Chemical Production Spółka Z Ograniczoną Odpowiedzialnością Method for reduction of emission of volatile organic compounds and the system for its execution
CN108358151A (en) * 2018-04-23 2018-08-03 中国化学赛鼎宁波工程有限公司 A kind of factory monitors with ethylene oxide, storage, recycling and handling system
CN108358151B (en) * 2018-04-23 2020-05-08 中国化学赛鼎宁波工程有限公司 Ethylene oxide monitoring, storing, recovering and loading and unloading system for factory

Similar Documents

Publication Publication Date Title
CN203355329U (en) Coarse vinyl chloride distillation system
CN101759590B (en) DMF recycling method
CN105214442A (en) A kind of new and effective recovery system for organic solvent
CN102115436B (en) Method for recovering acetone from dilute acetone water solution by reduced-pressure steam stripping type rectification
CN202191720U (en) Recovery device for tail gas of oxirane for polyether polyol
CN205549656U (en) Gaseous state solvent condensation recovery device
CN105214581A (en) The method of tail gas full-closed circulating recovery is polymerized in Production of PVC
CN103274360A (en) Chlorine gas and hydrogen chloride separating method
CN203816263U (en) Condensing and recycling equipment for volatile solvent
CN205300299U (en) Device of noncondensable gas in vertical condenser of desorption
CN203128457U (en) Device for removing saturated water in methane chloride
CN105031961A (en) Waste gas eliminating method and device in polyester resin production process
CN205042330U (en) Novel efficient organic solvent recovery system
CN210543451U (en) System tail gas recovery system glues
CN204815749U (en) Solvent recovery unit in tail gas
CN203030166U (en) High-purity hydrochloric acid tail gas recycling device
CN207385147U (en) A kind of environmental protection recycles tapping equipment with chemical industry tail gas
CN202044803U (en) High-vacuum condensing recovery system
CN202199141U (en) Vacuum plant for recycling solvent
CN206391826U (en) Landfill gas recovery and processing system
CN202829900U (en) Production equipment of poly(butylene succinate) (PBS)
CN201737874U (en) Secondary condensing plant for distillation in production of brominated epoxy resin
CN204502443U (en) For the liquid-ring vacuum pump system of Benzene Chloride rectification under vacuum
CN210251293U (en) Benzene vapor recovery device for trioxymethylene processing
CN204825007U (en) Condensing equipment is retrieved to mercury

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

Granted publication date: 20120418

Termination date: 20170909