CN102504225A - Vapor condensing and recovering device for use in production of polyester - Google Patents
Vapor condensing and recovering device for use in production of polyester Download PDFInfo
- Publication number
- CN102504225A CN102504225A CN2011103419988A CN201110341998A CN102504225A CN 102504225 A CN102504225 A CN 102504225A CN 2011103419988 A CN2011103419988 A CN 2011103419988A CN 201110341998 A CN201110341998 A CN 201110341998A CN 102504225 A CN102504225 A CN 102504225A
- Authority
- CN
- China
- Prior art keywords
- water
- vapor
- pipe
- communicated
- water 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.)
- Granted
Links
Images
Landscapes
- Polyesters Or Polycarbonates (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a vapor condensing and recovering device for use in production of polyester and belongs to the technical field of chemistry and mechanics. According to the vapor condensing and recovering device, the condensed water return water pipes of a vapor heating and heat tracing system are communicated with a vapor condensing water tank; and an upper set of nozzle and a lower set of nozzle are arranged in each condensed water return water pipe. The water inlet pipe of a multi-stage pump is led out from the lower part of a water tank. One path of the water outlet pipe of the multi-stage pump is communicated with a vapor generator and the other path of the water outlet pipe of the multi-stage pump is communicated with the nozzles of the condensed water return water pipe. The vapor condensing and recovering device is used to collect and recover 90 percent of the vapor sprayed by the multi-stage pump in a self-circular manner from the condensed water return water pipe, thereby circularly using the condensed water, reducing consumption of primary soft water and saving 60 cubic meters of water daily. As the heat of the vapor in the vapor condensing water tank is collected, the temperature of the water rises to about 80 DEG C from the original 50 DEG C, the water is conveyed to a vapor generator to be used circularly, the heat energy is comprehensively used, and the energy consumption is saved.
Description
Technical field: the present invention relates to the device for recovering tail gas in a kind of chemical plant production, belong to chemical machinery field.
Background technology: many materials are arranged for being prone to coagulated substance during polyester (PBT) is produced, for preventing process line by material obstructions of condensing, in the equipment in a large number pipelines used the water vapour of different pressures to accompany heat.The steam of three strands of different pressures converges at three main pipe lines behind drain valve, get into condensation water tank.Get into behind the condensation water tank in the steam water interface a large amount of steam and be not condensed and collect and be directly emitted, cause the loss of the water yield and heat.Keep the normal liquid level of vapour generator, just need continuous supplementation soft water.The direct discharging of this uncondensated steam causes the waste in about 20,000 sides water/year, also causes a large amount of energy dissipations simultaneously.
Summary of the invention: the objective of the invention is to design the vapour-condensing equipment for recovering in a kind of production of polyester, get up the moisture of steam and heat recovery and utilization, save energy and resource.For realizing this goal; Adopted such technical scheme: the vapour-condensing equipment for recovering in the production of polyester; Comprise steam-pipe, condensation water tank, multistage water pump and vapour generator; Each steam heating, tracing system condensate ruturn pipe are communicated with the vapor condensation water tank, and at least two group nozzles are installed in each condensate ruturn pipe.The part that condensate ruturn pipe is installed nozzle should be in vapor condensation water tank top, and is vertical direction.The water inlet pipe of multistage water pump is drawn from the bottom in the water tank, and the rising pipe one tunnel of multistage water pump is communicated with vapour generator, and another road is communicated with the nozzle in the condensate ruturn pipe.
The utilization of the vapour-condensing equipment for recovering in the production of polyester makes steam in the condensate ruturn pipe through multistage water pump self-circulation spray, and 90% recoverys that be captured realized recycling of water of condensation, reduced one-level soft usage quantity, day about 60m of the saving water yield
3The vapor condensation water tank has been because collected the heat of water vapour, and the temperature that makes water is elevated to about 80 ℃ from original 50 ℃, and high temperature soft water is delivered to vapour generator through stage pump and recycles, and has realized heat integration, energy efficient.
Description of drawings: Fig. 1 is the vapour-condensing equipment for recovering structural representation in the production of polyester.
Embodiment: be further described below in conjunction with accompanying drawing.
Vapour-condensing equipment for recovering in the production of polyester comprises steam-pipe, condensation water tank, multistage water pump and vapour generator.The companion of each steam heating, tracing system is hot, heat form is different, temperature, pressure difference, and companion's heat, heating completion rear section vapor condensation Cheng Shui still have the steam of considerable part to have higher temperature.Condensate ruturn pipe 2 is communicated with vapor condensation water tank 1, and two groups of nozzles 3 up and down are installed in each condensate ruturn pipe.The part that condensate ruturn pipe is installed nozzle should be in vapor condensation water tank top, and is vertical direction.Water vapor condenses into water under the spiral water smoke cooling of nozzle ejection, reduced soft consumption.The heat of water vapor has improved the temperature of water in the condensation water tank simultaneously, and no longer runs off along with discharge of steam.The water inlet pipe of multistage water pump 4 is drawn from the bottom in the water tank.The rising pipe one tunnel of multistage water pump is communicated with the nozzle of condensate ruturn pipe, and another road of multistage pumping line is communicated with vapour generator 5, high-temperature water is sent into vapour generator saved energy consumption.
Claims (2)
1. the vapour-condensing equipment for recovering in the production of polyester; Comprise steam-pipe, condensation water tank, multistage water pump and vapour generator; It is characterized in that: the condensate ruturn pipe of each steam heating, tracing system (2) is communicated with vapor condensation water tank (1) in the production of polyester; Nozzle (3) is installed in condensate ruturn pipe, and the water inlet pipe of multistage water pump is drawn from the bottom in the water tank; The rising pipe one tunnel of multistage water pump is communicated with vapour generator (5), and another road is communicated with the nozzle of condensate ruturn pipe.
2. the vapour-condensing equipment for recovering in the production of polyester as claimed in claim 1 is characterized in that: nozzle (3) is installed in each condensate ruturn pipe (2), and installs upper and lower at least two groups; The part that condensate ruturn pipe is installed nozzle should be in vapor condensation water tank top, and is vertical direction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201110341998 CN102504225B (en) | 2011-10-23 | 2011-10-23 | Vapor condensing and recovering device for use in production of polyester |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201110341998 CN102504225B (en) | 2011-10-23 | 2011-10-23 | Vapor condensing and recovering device for use in production of polyester |
Publications (2)
Publication Number | Publication Date |
---|---|
CN102504225A true CN102504225A (en) | 2012-06-20 |
CN102504225B CN102504225B (en) | 2013-06-05 |
Family
ID=46216364
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 201110341998 Active CN102504225B (en) | 2011-10-23 | 2011-10-23 | Vapor condensing and recovering device for use in production of polyester |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102504225B (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103275347A (en) * | 2013-05-29 | 2013-09-04 | 新疆蓝山屯河聚酯有限公司 | Recovery device in PET resin continuous polymerization equipment |
CN103768822A (en) * | 2012-10-23 | 2014-05-07 | 中国石油化工股份有限公司 | Treatment method of unsaturated polyester steam |
CN109661542A (en) * | 2016-08-26 | 2019-04-19 | 扬·K·允 | Boiler feedwater case energy recycling system |
CN112781291A (en) * | 2019-10-22 | 2021-05-11 | 广州科勒尔制冷设备有限公司 | Multifunctional ice slurry storage, stirring and pumping system |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN87103241A (en) * | 1986-04-29 | 1987-11-11 | 卡尔弗沙工业设备公司 | The production technique of high molecular weight polyesters and device thereof |
US20040171789A1 (en) * | 2001-05-25 | 2004-09-02 | Randolf Reimann | Method and device for the production polyethyleneterephthalate |
-
2011
- 2011-10-23 CN CN 201110341998 patent/CN102504225B/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN87103241A (en) * | 1986-04-29 | 1987-11-11 | 卡尔弗沙工业设备公司 | The production technique of high molecular weight polyesters and device thereof |
US20040171789A1 (en) * | 2001-05-25 | 2004-09-02 | Randolf Reimann | Method and device for the production polyethyleneterephthalate |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103768822A (en) * | 2012-10-23 | 2014-05-07 | 中国石油化工股份有限公司 | Treatment method of unsaturated polyester steam |
CN103768822B (en) * | 2012-10-23 | 2016-06-22 | 中国石油化工股份有限公司 | A kind of processing method of unsaturated polyester (UP) steam |
CN103275347A (en) * | 2013-05-29 | 2013-09-04 | 新疆蓝山屯河聚酯有限公司 | Recovery device in PET resin continuous polymerization equipment |
CN103275347B (en) * | 2013-05-29 | 2016-02-10 | 新疆蓝山屯河聚酯有限公司 | Retrieving arrangement in PET resin continuous polymerization device |
CN109661542A (en) * | 2016-08-26 | 2019-04-19 | 扬·K·允 | Boiler feedwater case energy recycling system |
CN109661542B (en) * | 2016-08-26 | 2020-03-10 | 扬·K·允 | Energy recovery system for boiler water supply tank |
CN112781291A (en) * | 2019-10-22 | 2021-05-11 | 广州科勒尔制冷设备有限公司 | Multifunctional ice slurry storage, stirring and pumping system |
Also Published As
Publication number | Publication date |
---|---|
CN102504225B (en) | 2013-06-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102010020B (en) | Solar energy sea water desalinization heat collecting system | |
CN105423266B (en) | A kind of high/low temperature sewage remaining energy cascade utilization and recycling reclaiming system and its method | |
CN102504225B (en) | Vapor condensing and recovering device for use in production of polyester | |
CN206607044U (en) | A kind of thermal power plant's exhaust steam residual heat utilizes device | |
CN201193222Y (en) | Oil production device of oil shale retort | |
CN205084431U (en) | Multiple -effect falling film evaporation ware | |
CN102889776B (en) | Cyclic utilization production device of waste gas and steam of dryer | |
CN205031921U (en) | Strip tower flash steam's heat energy and solvent recycling system | |
CN204275521U (en) | A kind of liquid ammonia gasification dry evaporator | |
CN101131234A (en) | Waste-heat recovery technology for turbine exhaust steam in electric power plant | |
CN202813338U (en) | Steam condensate reclaiming system | |
CN203170033U (en) | Multi-stage evaporation tower for carrying out evaporation treatment on brackish water by utilizing air | |
CN202902824U (en) | Waste heat steam cyclic utilization production device of drier | |
CN204767471U (en) | With high -temperature gas concentrate system all | |
CN101226032A (en) | Waste steam utilization equipment | |
CN204454674U (en) | Waste water air-lift device | |
CN204447354U (en) | Multi-effect evaporator | |
CN202040542U (en) | Condensate recycling device of steam heater of molecular sieve | |
CN206746021U (en) | A kind of water coal slurry pressure gasification dirt vapor recovery utilizes device | |
CN103691139A (en) | Residual heat heating system for evaporator | |
CN101434847A (en) | Oil shale retort oil extraction process | |
CN204881253U (en) | Steam condensate water recycle system | |
CN108105752A (en) | The coal consumption of power supply of thermal power plant is down to below 200g/kw.h and emission reduction | |
CN103643431A (en) | Steam circulating system | |
CN204005938U (en) | Environmental-protection energy-saving device is reclaimed in injecting type exhaust steam |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20171127 Address after: 831800 the Xinjiang Uygur Autonomous Region Hui Autonomous Prefecture of Qitai County Changji Lama Lake Industrial Park Lanshan Tun River Energy Co., Ltd. Patentee after: XINJIANG LANSHAN TUNHE ENERGY CO., LTD. Address before: No. 316 Beijing South Road, Changji, the Xinjiang Uygur Autonomous Region Patentee before: Xinjiang Blue Ridge Tunhe Polyester Co., Ltd. |
|
TR01 | Transfer of patent right |