CN209540861U - A kind of condensate liquid step recyclable device - Google Patents

A kind of condensate liquid step recyclable device Download PDF

Info

Publication number
CN209540861U
CN209540861U CN201822133757.4U CN201822133757U CN209540861U CN 209540861 U CN209540861 U CN 209540861U CN 201822133757 U CN201822133757 U CN 201822133757U CN 209540861 U CN209540861 U CN 209540861U
Authority
CN
China
Prior art keywords
flash tank
liquid
communicated
condensate
inlet
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.)
Active
Application number
CN201822133757.4U
Other languages
Chinese (zh)
Inventor
魏聚广
刘金贵
赵韵
文培娜
李爱国
朱建强
崔曼丽
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.)
XINXIANG ZHONGXIN CHEMICAL CO Ltd
Original Assignee
XINXIANG ZHONGXIN 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 XINXIANG ZHONGXIN CHEMICAL CO Ltd filed Critical XINXIANG ZHONGXIN CHEMICAL CO Ltd
Priority to CN201822133757.4U priority Critical patent/CN209540861U/en
Application granted granted Critical
Publication of CN209540861U publication Critical patent/CN209540861U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The utility model provides a kind of condensate liquid step recyclable device, including high temperature condensate line and cryogenic condensation liquid pipe, the liquid outlet of high temperature condensate line is communicated with the inlet of the first flash tank, and the expansion slot top exit of the first flash tank setting is communicated with after check valve with high-temperature steam pipe network by the road;The liquid outlet of first flash tank is communicated through drain valve with the first inlet of the second flash tank, the liquid outlet of cryogenic condensation liquid pipe is communicated with the second inlet of the second flash tank, the expansion slot top exit of second flash tank setting is communicated with indoor heating system for steam ports, and the leakage fluid dram of the second flash tank divides two-way to be connected respectively with boiler feed, plate heat exchanger through condensate liquid booster pump.The high and low temperature steam condensate generated to system combs, and carries out two-stage decompression expansion to by high temperature condensate liquid, the low-pressure steam that first order expansion generates is for heat tracing, heat preservation;For the low-pressure steam that second level expansion generates for heating, heating, life, cooling, rational technology, effect are good.

Description

A kind of condensate liquid step recyclable device
Technical field
The utility model relates to the high, medium and low temperature condensate liquid step reclaimers that chemical plant installations generates, and in particular to a kind of Condensate liquid step recyclable device.
Background technique
Condensate liquid results from steam during heating and conveying, thus it not only water quality it is good and also contain big calorimetric Amount, the high-temperature condensation water of condensate liquid recovery system recovered steam system discharge, can maximally utilise the heat of condensate liquid, save Water is about used, fuel is saved.
Currently, condensate liquid recovery process is broadly divided into Recovery with Open-loop system and two kinds of closed-style recycling system.
1, Recovery with Open-loop system is that condensate liquid is recovered in header tank, during the recycling of condensate liquid and utilization, is returned The open at one end on closed tube road is open to atmosphere to atmosphere, the i.e. header tank of condensate liquid.When the pressure of condensed water is lower, by pressing certainly not When can reach recycling place, force feed is carried out to condensed water using high-temperature water pump.The advantages of this system is that equipment is simple, operation Convenient, initial outlay is small;But system footprint area is big, resulting deficiency in economic performance, environmental pollution are larger, and due to condensation Liquid is directly contacted with atmosphere, and the oxyty in condensed water improves, and is also easy to produce equipment corrosion.
2 closed-style recycling systems are condensed water header tank and all pipelines all in constant direct draught, and system is closing 's.Energy possessed by condensed water largely passes through certain reclaimer and is directly recovered in boiler in system, condensed water Recovered temperature is only lost in pipe network cooling part, and due to closing, water quality is guaranteed, reduces the water process expense recycled into boiler With.Its advantage is that condensing hot air furnace is good in economic efficiency, the long working life of equipment, but the initial outlay of system is relatively large, It is inconvenient for operation.
The heat and power for how utilizing steam condensate to greatest extent, make high-grade steam condensate liquid and low-grade condensation Liquid can be recycled properly, improve the effect of condensate liquid recycling, and easy to operate, reasonable, with low investment, be the skill of a urgent need to resolve Art problem.
Summary of the invention
For the problems of the prior art, the utility model provides a kind of condensate liquid step recyclable device.
A kind of condensate liquid step recyclable device, it is characterised in that: described including high temperature condensate line and cryogenic condensation liquid pipe The liquid outlet of high temperature condensate line is communicated with the inlet of the first flash tank, is gone out at the top of the expansion slot of the first flash tank setting Mouth is communicated with after check valve with high-temperature steam pipe network by the road;The liquid outlet of first flash tank is flashed through drain valve and second First inlet of tank communicates, and the liquid outlet of the cryogenic condensation liquid pipe is communicated with the second inlet of second flash tank, The expansion slot top exit of the second flash tank setting is communicated with indoor heating system for steam ports, second flash tank Leakage fluid dram divides two-way to be connected respectively with boiler feed, plate heat exchanger through condensate liquid booster pump.
Further are as follows: the liquid outlet and desalted water condensate liquid water tank of the plate heat exchanger or the inlet of desalted water mixed bed It communicates.
Further are as follows: switch valve pipeline is parallel on the drain valve.
The utility model has the beneficial effects that the high and low temperature steam condensate generated to system combs, to high temperature is cold Lime set carries out two-stage decompression expansion, and the low-pressure steam that first order expansion generates is for heat tracing, heat preservation;Second level expansion generates low Press steam for heating, heating, life, cooling, rational technology, using effect are good.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Specific embodiment
It elaborates with reference to the accompanying drawing to the utility model.It should be noted that a left side in the example of the utility model, In, the positional terms such as right, upper and lower, be only relative concept or be to refer to the normal operating condition of product each other, without answering This is considered restrictive.
As shown in Figure 1, a kind of condensate liquid step recyclable device, including high temperature condensate line B and cryogenic condensation liquid pipe C, institute The liquid outlet for stating high temperature condensate line B communicates by the road, after valve with the inlet of the first flash tank 1, first flash tank 1 11 top exit of expansion slot of setting is communicated with after check valve 15 with high-temperature steam pipe network A by the road;First flash tank 1 Liquid outlet is communicated through drain valve 12 with the first inlet of the second flash tank 2, and the liquid outlet of the cryogenic condensation liquid pipe C is through pipe It is communicated after road, valve with the second inlet of second flash tank 2,22 top of expansion slot that second flash tank 2 is arranged Outlet is communicated with indoor heating system F's for steam ports, and the leakage fluid dram of second flash tank 2 divides two-way through condensate liquid booster pump 31 It is connected respectively with boiler feed G, plate heat exchanger 32;The sewage draining exit 14 of first flash tank 1 is communicated with dirt discharge groove D, and second dodges The sewage draining exit 21 of steaming pot 2 is communicated with the second dirt discharge groove E;Wherein, the liquid outlet of the plate heat exchanger 32 and desalted water condensate liquid The inlet of water tank K or desalted water mixed bed K communicate;13 pipeline of switch valve is parallel on the drain valve 12.
The basic principles and main features and advantage of the utility model have been shown and described above.The technical staff of the industry It should be appreciated that the present utility model is not limited to the above embodiments, the above embodiments and description only describe this The principle of utility model, on the premise of not departing from the spirit and scope of the utility model, the utility model also has various change And improvement, these various changes and improvements fall within the scope of the claimed invention.The utility model requires protection scope It is defined by the appending claims and its equivalent thereof.

Claims (3)

1. a kind of condensate liquid step recyclable device, it is characterised in that: including high temperature condensate line and cryogenic condensation liquid pipe, the height The liquid outlet of warm condensate line is communicated with the inlet of the first flash tank, the expansion slot top exit of the first flash tank setting It is communicated by the road with after check valve with high-temperature steam pipe network;The liquid outlet of first flash tank is through drain valve and the second flash tank The first inlet communicate, the liquid outlet of the cryogenic condensation liquid pipe is communicated with the second inlet of second flash tank, institute State the expansion slot top exit of the second flash tank setting and communicating for steam ports for indoor heating system, the row of second flash tank Liquid mouth divides two-way to be connected respectively with boiler feed, plate heat exchanger through condensate liquid booster pump.
2. a kind of condensate liquid step recyclable device according to claim 1, it is characterised in that: the plate heat exchanger goes out Liquid mouth is communicated with the inlet of desalted water condensate liquid water tank or desalted water mixed bed.
3. a kind of condensate liquid step recyclable device according to claim 1 or 2, it is characterised in that: on the drain valve It is parallel with switch valve pipeline.
CN201822133757.4U 2018-12-18 2018-12-18 A kind of condensate liquid step recyclable device Active CN209540861U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201822133757.4U CN209540861U (en) 2018-12-18 2018-12-18 A kind of condensate liquid step recyclable device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201822133757.4U CN209540861U (en) 2018-12-18 2018-12-18 A kind of condensate liquid step recyclable device

Publications (1)

Publication Number Publication Date
CN209540861U true CN209540861U (en) 2019-10-25

Family

ID=68264828

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201822133757.4U Active CN209540861U (en) 2018-12-18 2018-12-18 A kind of condensate liquid step recyclable device

Country Status (1)

Country Link
CN (1) CN209540861U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113188181A (en) * 2021-03-29 2021-07-30 大唐七台河发电有限责任公司 Heating drainage recovery device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113188181A (en) * 2021-03-29 2021-07-30 大唐七台河发电有限责任公司 Heating drainage recovery device

Similar Documents

Publication Publication Date Title
CN102734787B (en) Concurrent recycling system for boiler smoke afterheat
CN102032612A (en) Cogeneration energy-saving device and method using residual heat of direct air-cooling unit to supply heat
CN107559928A (en) A kind of efficient heating system and its compressing type heat-exchange unit based on low-temperature waste heat
CN201265955Y (en) High temperature water heating system by waste heat recovery
CN102022770A (en) Heat and power cogeneration energy-saving device and method for supplying heat by using direct waste heat of air-cooling unit
CN107218094A (en) A kind of multiple pressure flashes the device of organic Rankine bottoming cycle cogeneration
CN104296554A (en) Steam condensing type power station steam condenser chamber vacuumizing system
CN102419031B (en) Superhigh-temperature heat pump device and use method
CN209540861U (en) A kind of condensate liquid step recyclable device
CN205351277U (en) A back pressure steam turbine thermodynamic system for isolated network operation
CN86105222A (en) Utilize the low-pressure energy-saving hybrid system of smoke discharging residual heat
CN201779684U (en) High-grade recycling system for exhaust heat of power station boiler
CN203848505U (en) Device for recovering condensation heat energy of gas boiler flue gas by means of heat pump
CN201836967U (en) Cogeneration energy saving device utilizing waste heat of direct air cooling unit for heat supply
CN103954039A (en) Device and method for recycling smoke condensate heat energy of gas boiler in heat pumping mode
CN202692016U (en) Flue gas waste heat recovery system for concurrent boiler
CN206874322U (en) A kind of device of multiple pressure flash distillation organic Rankine bottoming cycle cogeneration
CN202974001U (en) Sub-control phase-change heat exchange system based on grading combined heat exchange
CN201836968U (en) Cogeneration energy saving device utilizing waste heat of indirect air cooling unit for heat supply
CN202382481U (en) Super-high temperature heat pump device
CN203183716U (en) Alcohol distillation device with heat recovery device
CN207081361U (en) A kind of system that stable hot water is provided using residual heat from boiler fume
CN201836969U (en) Cogeneration energy-saving device supplying heat by utilizing residual heat of direct air-cooling unit
CN202250270U (en) Steam turbine condensing system
CN206257647U (en) A kind of non-clean Steam Recovery utilization system of injecting type

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant