CN106524112A - Jet type uncleanly steam recovery and comprehensive utilization system - Google Patents
Jet type uncleanly steam recovery and comprehensive utilization system Download PDFInfo
- Publication number
- CN106524112A CN106524112A CN201611168958.7A CN201611168958A CN106524112A CN 106524112 A CN106524112 A CN 106524112A CN 201611168958 A CN201611168958 A CN 201611168958A CN 106524112 A CN106524112 A CN 106524112A
- Authority
- CN
- China
- Prior art keywords
- steam
- injecting type
- shell
- utilization system
- heat exchanger
- 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.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B31/00—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus
- F22B31/08—Installation of heat-exchange apparatus or of means in boilers for heating air supplied for combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
- F22B37/38—Determining or indicating operating conditions in steam boilers, e.g. monitoring direction or rate of water flow through water tubes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D11/00—Feed-water supply not provided for in other main groups
- F22D11/02—Arrangements of feed-water pumps
- F22D11/06—Arrangements of feed-water pumps for returning condensate to boiler
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Water Supply & Treatment (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention relates to a steam recovery and utilization system and discloses a jet type uncleanly steam recovery and comprehensive utilization system. The problems that most of uncleanly steam in existing industrial production workshops is directly exhausted to the atmosphere, steam afterheat is wasted, and the exhausted steam can pollute the environment are solved. According to the jet type uncleanly steam recovery and comprehensive utilization system, a shell and tube heat exchanger is in seal connection with an industrial production workshop and is connected with a plate heat exchanger; the plate heat exchanger is connected with an acid collection tank and a water collection tank; the water collection tank is connected with a steam boiler and the shell and tube heat exchanger; the shell and tube heat exchanger is connected with a water inlet in the side wall of a flash tank; the flash tank is connected with a condenser; the condenser is connected with a jet type unit and the water collection tank; one end of the jet type unit is connected with the steam boiler, and the other end of the jet type unit is connected with the industrial production workshop; and the flash tank is connected with the water collection tank. The jet type uncleanly steam recovery and comprehensive utilization system is used for recovery and comprehensive utilization of steam of the industrial production workshop.
Description
Technical field
The present invention relates to a kind of commercial production workshop Steam Recovery utilization system, specifically related to a kind of injecting type is non-clear
Clean Steam Recovery utilization system.
Background technology
The energy is the important substance basis of human survival and development, the occupancy volume per person of the energy, the composition of the energy, the energy
Utilization rate is often as one national modernization level of measurement.Steam is as a kind of cleaning, safe energy carrier each
Be widely used in each industry of row, such as generating, oil, chemical industry, printing and dyeing, papermaking, light textile, brewage, the industrial circle such as rubber, potting
In.After steam releases the latent heat of vaporization in each gas utilization unit, it is changed into saturation condensate of the intimate equality of temperature with pressure, due to steam
It is more than atmospheric pressure using pressure, so the heat that has of condensate is up to the 20%～30% of the full heat of steam, and pressure,
The heat that the higher condensate of temperature has is more, and the ratio for accounting for steam total amount of heat is also bigger.As can be seen that reclaim condensing
The heat of water, and effectively utilizes in addition, with very big energy-saving potential.Condensation water recovery system is broadly divided into Recovery with Open-loop system
Two kinds of system and closed-style recycling system.During Recovery with Open-loop system is the feedwater tank condensing hot air furnace to boiler, returning in condensed water
During receiving and utilizing, the open at one end of recovery pipe is open to air to the header tank of air, i.e. condensed water.When condensed water
Pressure is relatively low, during by reaching recycling place from pressure, carries out force feed using high-temperature water pump to condensed water.But system footprint
Area is big, and the deficiency in economic performance of gained, environmental pollution are larger, and, in condensed water. due to condensed water directly and atmosphere
Oxyty is improved, and is also easy to produce equipment corrosion.Closed-style recycling system is condensed water header tank and all pipelines all in constant
Direct draught, system be closing.The energy major part that condensed water has in system is directly returned by certain reclaimer
Receive in boiler, the recovered temperature of condensed water is only lost in pipe network cooling part, as closing, water quality are guaranteed, reduce back
Take in the water process expense of boiler.Its advantage is the good in economic efficiency of condensing hot air furnace, the long working life of equipment, but system
Initial outlay it is relatively large, inconvenient operation.
The non-clean steam that especially traditional alcoholic workshop produces is directly discharged in air, on the one hand, waste steaming
The waste heat of vapour；On the other hand, the humble and shabby steam that alcoholic workshop produces is unprocessed, is exhausted directly to cause environment in the middle of air
Pollution.
To sum up, the most of non-clean steam in existing commercial production workshop is directly discharged in air, not only wastes steam
Waste heat, and also there is pollution environment in institute's aerofluxuss body.
The content of the invention
The invention aims to the most of non-clean steam for solving existing commercial production workshop is directly discharged to greatly
In gas, steam waste heat is not only wasted, and institute's aerofluxuss body also there is a problem of polluting environment.And then it is non-clear to provide a kind of injecting type
Clean Steam Recovery utilization system.
The technical scheme is that：
A kind of non-clean Steam Recovery utilization system of injecting type, it includes steam boiler, flash tank, shell-tube type heat exchange
Device, filling of catchmenting, plate type heat exchanger, injecting type unit, collection acid filling, condenser and multiple water pumps,
Steam drain of the air intake of shell and tube exchanger by a segment pipe with commercial production workshop is tightly connected, shell-tube type
First outlet of heat exchanger is connected with the water inlet of plate type heat exchanger by a segment pipe, and shell and tube exchanger is changed with board-like
A water pump and a dynamic valve is provided between hot device, and the acid discharge hole of plate type heat exchanger is filled with collection acid by a segment pipe and is connected,
The outlet of plate type heat exchanger is connected with the first water inlet of filling of catchmenting, and the first outlet of filling of catchmenting passes through a segment pipe and steaming
Boiler furnace connects, and catchments and is provided with a water pump and a dynamic valve between filling and steam boiler, and the second outlet of filling of catchmenting leads to
Cross a segment pipe to be connected with shell and tube exchanger, to catchment and a water pump and a power is provided between filling and shell and tube exchanger
Valve, the second outlet of shell and tube exchanger are connected with the water inlet on flash distillation pot sidewall, the upper end venthole of flash tank with it is cold
The top air intake connection of condenser, the upper end of condenser is connected with injecting type unit lower end by a segment pipe, under condenser
End is connected with catchmenting to fill by a segment pipe, and one end of injecting type unit is connected with the venthole of steam boiler, injecting type unit
The other end be connected with the air intake in commercial production workshop, the lower end outlet of flash tank passes through a segment pipe and catchments under filling
The second water inlet is held to connect, flash tank and the pipeline between filling that catchments are provided with a water pump and two dynamic valves, two power
Valve be separately mounted to the flash tank and catchment fill between pipeline on.
Further, it also includes butterfly valve, and butterfly valve is connected in parallel on injecting type unit by pipeline.
Further, the pipeline between steam boiler and injecting type unit is provided with dynamic valve, temperature sensor and pressure
Sensor.
Further, dynamic valve is arranged on pipeline between steam boiler and injecting type unit, temperature sensor and pressure
Force transducer is installed in the steam outlet of steam boiler.
Further, the pipeline between injecting type unit and commercial production workshop be provided with dynamic valve, temperature sensor and
Pressure transducer.
Further, the upper end of flash tank is provided with temperature sensor and pressure transducer.
Further, the pipeline between shell and tube exchanger and plate type heat exchanger is provided with temperature sensor.
Further, the pipeline between commercial production workshop and shell and tube exchanger is provided with temperature sensor.
Further, temperature sensor is provided with the acid discharge mouth of plate type heat exchanger.
Further, it also includes two fluid level measuring instruments, and two fluid level measuring instruments are separately mounted to the upper end of flash tank
In the middle part of sliding channel of filling of catchmenting.
The present invention is had the effect that compared with prior art：
1st, the system adopts high temperature and high pressure steam for driving, and with shell and tube exchanger as intermediary, enters in injecting type unit
The recovery of the non-clean steam heat of row, is industrial supply with the steam of steam boiler jointly after recovery.
2nd, the non-clean steam collected carries out heat exchange into the diversion of shell and tube exchanger and injecting type unit and is changed into cold
Solidifying water, condensed water in the presence of water pump enters plate type heat exchanger and low temperature softening water is exchanged heat, and after heat exchange, condensed water is reduced to
Low temperature sour water is discharged.The diversion of injecting type unit is flowed through after shell and tube exchanger heats up and is changed into low-pressure steam into ejector machine group
System is continued as after the high steam mixing produced with steam boiler steam is provided.So ensureing not changing system conditions
In the case of, both accomplished all to reclaim acid discharge steam waste heat, realized acid and the separation of heat again.
3rd, after adding injecting type unit, softened water first flows through plate type heat exchanger, the softening current direction water collect tank after intensification.One
Aspect, the water into water collect tank continue as steam boiler water supply, improve the thermal efficiency of steam boiler；On the other hand, into collection
The water of water pot is water pump water-supply and pressure-stabling.
4th, the water-break of the softened water and injecting type unit Jing after plate type heat exchanger intensification is all 30 DEG C, this ensure that system
Relative thermodynamic equilibrium, make system operation more stable.
5th, the purpose of water collect tank is to realize that softened water and the pressure of injecting type unit water system separate, and can soften water transport again
In the case that row is unstable, it is ensured that the normal operation of injecting type system.Heat Calculation is reclaimed by injecting type unit, is produced per hour
Quantity of steam be more than 4 tons, in steam boiler underrun, per hour produce quantity of steam be more than 16 tons, existing steam
The heat capacity of boiler disclosure satisfy that the demand of system operation.
Description of the drawings
Fig. 1 is the flow chart of the present invention；
Fig. 2 is the structural representation of flash tank 2；
Fig. 3 is the structural representation of shell and tube exchanger 3；
Fig. 4 is the structural representation for filling 4 that catchments；
Fig. 5 is the structural representation of plate type heat exchanger 5.
Specific embodiment
Specific embodiment one：With reference to Fig. 1, Fig. 2, Fig. 3, Fig. 4 and Fig. 5 illustrate present embodiment, the one of present embodiment
The non-clean Steam Recovery utilization system of injecting type is planted, it includes steam boiler 6, it also exchanges heat including flash tank 2, shell-tube type
Device 3, filling 4 of catchmenting, plate type heat exchanger 5, injecting type unit 7, collection acid fill 11, condenser 12 and multiple water pumps 8,
Steam drains of the air intake 3-1 of shell and tube exchanger 3 by a segment pipe with commercial production workshop 1 is tightly connected,
First outlet 3-2 of shell and tube exchanger 3 is connected with the water inlet 5-1 of plate type heat exchanger 5 by a segment pipe, and shell-tube type
A water pump 8 and a dynamic valve is provided between heat exchanger 3 and plate type heat exchanger 5, and the acid discharge hole 5-3 of plate type heat exchanger 5 passes through
One segment pipe fills 11 with collection acid and is connected, and the outlet 5-2 of plate type heat exchanger 5 is connected with the first water inlet 4-2 of filling 4 of catchmenting, and is collected
Water is filled 4 the first outlet 4-1 and is connected with steam boiler 6 by a segment pipe, to be catchmented and be provided with one between filling 4 and steam boiler
Water pump 8 and a dynamic valve, the second outlet 4-3 of filling 4 of catchmenting are connected with shell and tube exchanger 3 by a segment pipe, are catchmented
Fill a water pump 8 and a dynamic valve, the second outlet 3-3 of shell and tube exchanger 3 is provided between 4 and shell and tube exchanger 3
It is connected with the water inlet on 2 side wall of flash tank, the upper end venthole of flash tank 2 is connected with the top air intake of condenser 12, cold
The upper end of condenser 12 is connected with 7 lower end of injecting type unit by a segment pipe, and the lower end of condenser 12 passes through a segment pipe and collection
Water fills 4 and connects, and one end of injecting type unit 7 is connected with the venthole of steam boiler 6, the other end and the industry of injecting type unit 7
The air intake connection of workshop 1, the lower end outlet 2-3 of flash tank 2 are passed through a segment pipe and are entered with the lower end second of filling 4 of catchmenting
Mouth of a river 4-4 connects, and flash tank 2 and the pipeline filled between 4 that catchments are provided with a water pump 8 and two dynamic valves, two dynamic valves
It is separately mounted to the flash tank 2 and catchments on the pipeline filled between 4.
Specific embodiment two：Present embodiment is illustrated with reference to Fig. 1, present embodiment also includes butterfly valve 9, and butterfly valve 9 passes through
Pipeline is connected in parallel on injecting type unit 7.It is arranged such, cut-out and throttling action can be played, industrial life can be efficiently controlled
Produce the steam flow in the connecting pipe between workshop 1 and steam boiler 6.Other compositions and annexation and specific embodiment
One is identical.
Specific embodiment three：Present embodiment, the steam boiler 6 of present embodiment and ejector machine are illustrated with reference to Fig. 1
Pipeline between group 7 is provided with dynamic valve, temperature sensor and pressure transducer.It is arranged such, can effectively monitors steam
High steam temperature value and high-pressure steam pressure value that boiler 6 is produced.Other compositions and annexation and specific embodiment one
Or two is identical.
Specific embodiment four：Present embodiment is illustrated with reference to Fig. 1, the dynamic valve of present embodiment is arranged on steam boiler
On pipeline between 6 and injecting type unit 7, temperature sensor is installed in the steam (vapor) outlet of steam boiler 6 with pressure transducer
Place.Other compositions and annexation and specific embodiment one, two or three are identical.
Specific embodiment five：Present embodiment, the injecting type unit 7 of present embodiment and industry life are illustrated with reference to Fig. 1
The pipeline produced between workshop 1 is provided with dynamic valve, temperature sensor and pressure transducer.It is arranged such, effectively can monitors
The vapor (steam) temperature value and vapour pressure force value of the steam collected to the steam drain from injecting type unit 7.Other compositions and connection are closed
System is identical with specific embodiment one, two, three or four.
Specific embodiment six：Present embodiment is illustrated with reference to Fig. 1, the upper end of the flash tank 2 of present embodiment is provided with temperature
Degree sensor and pressure transducer.It is arranged such, can effectively monitors vapor (steam) temperature value and the steam pressure in flash tank 2
Value.Other compositions and annexation and specific embodiment one, two, three, four or five are identical.
Specific embodiment seven：Present embodiment, the shell and tube exchanger 3 of present embodiment and board-like are illustrated with reference to Fig. 1
Pipeline between heat exchanger 5 is provided with temperature sensor.It is arranged such, can effectively monitors from shell and tube exchanger 3
The water temperature of one water outlet.Other compositions and annexation and specific embodiment one, two, three, four, five or six are identical.
Specific embodiment eight：Present embodiment, present embodiment commercial production workshop 1 and shell-tube type are illustrated with reference to Fig. 1
Pipeline between heat exchanger 3 is provided with temperature sensor.It is arranged such, effectively can monitors from commercial production workshop 1
The vapor (steam) temperature value that steam drain is collected.Other compositions and annexation and specific embodiment one, two, three, four, five, six or
Seven is identical.
Specific embodiment nine：Present embodiment, the acid discharge mouth of the plate type heat exchanger 5 of present embodiment are illustrated with reference to Fig. 1
Place is provided with temperature sensor.It is arranged such, can effectively monitors the temperature of the sour water discharged at the acid discharge mouth of plate type heat exchanger 5
Value, it is to avoid the waste of waste heat and the pollution to environment.Other compositions and annexation and specific embodiment one, two, three, four,
5th, six, seven or eight are identical.
Specific embodiment ten：Present embodiment is illustrated with reference to Fig. 1, present embodiment also includes two fluid level measuring instruments
10, two fluid level measuring instruments 10 are separately mounted on the upper end and the middle part of sliding channel for filling 4 of catchmenting of flash tank 2.It is arranged such, can
The level value and the level value for filling 4 that catchments of flash tank 2 are monitored effectively.Other compositions and annexation and specific embodiment
First, two, three, four, five, six, seven, eight or nine are identical.
Embodiment：
The present embodiment is illustrated to this embodiment with reference to Fig. 1 by taking the alcoholic workshop in commercial production workshop as an example,
The system adopts high temperature and high pressure steam for driving, with shell and tube exchanger 3 as intermediary, enters in injecting type unit 7
The recovery of the non-clean steam heat of row.
99.6 DEG C of non-clean steam that the steam drain in alcoholic workshop is collected enter shell and tube exchanger 3 and injecting type unit
7 diversion carries out the condensed water for being changed into 90 DEG C that exchanges heat, and condensed water in the presence of water pump 8 enters plate type heat exchanger 5 and low temperature is soft
Change water to be exchanged heat, after heat exchange, condensed water is reduced to 10 DEG C of sour water discharges.
The air pressure of the existing steam (vapor) outlet of steam boiler 6 be 0.8MPa, steamer pressure be 0.2MPa to 0.4MPa, boiler soften
Water carrys out coolant-temperature gage for 8 DEG C.Softened water first flows through plate type heat exchanger 5, heats up as 30 DEG C, flows to water collect tank 4, into water collect tank 4
Water, on the one hand continues as steam boiler water supply, improves the thermal efficiency of steam boiler；On the other hand it is 8 water-supply and pressure-stabling of water pump.
The softened water of 30 DEG C of water collect tank 4 flows into shell and tube exchanger 3 in the presence of water pump 8, exchanges heat through shell-tube type
Device 3 rises to 40 DEG C and enters condenser 12 into after 2 flash distillation of flash tank after exchanging heat, the condensed water into condenser 12 enters injection
It is changed into negative pressure steam after 7 injection of formula unit, the high steam produced with steam boiler 6 is continued as system and provides steam after mixing.
Softened water in flash tank 2 is flowed in water collect tank 4 in the presence of water pump 8, and condensate comes back to water collect tank.
To sum up, in the case where ensureing not changing whole system operating condition, both accomplished acid discharge steam waste heat whole
Reclaim, realize acid and the separation of heat again.
Operation principle：
With reference to Fig. 1, the non-clean steam that commercial production workshop 1 is discharged enters shell and tube exchanger 3, Jing and injecting type unit
Condense into plate type heat exchanger 5 after the water heat exchange of 7 backflows and drain after being exchanged heat with 6 moisturizing of steam boiler.Steam boiler moisturizing
Enter, give birth to industry into shell and tube exchanger 3 all the way
Produce workshop 1 discharge non-clean steam exchanged heat after enter 2 flash distillation of flash tank after enter condenser 12, the steam after injection with
The steam out of steam boiler 6 enters workshop, and condensate comes back to water collect tank 4.
Claims (10)
1. the non-clean Steam Recovery utilization system of a kind of injecting type, it includes steam boiler (6), it is characterised in that：It is also
Fill including flash tank (2), shell and tube exchanger (3), filling (4) of catchmenting, plate type heat exchanger (5), injecting type unit (7), collection acid
(11), condenser (12) and multiple water pumps (8),
Steam drain sealing of the air intake (3-1) of shell and tube exchanger (3) by a segment pipe with commercial production workshop (1) connects
Connect, first outlet (3-2) of shell and tube exchanger (3) is connected by the water inlet (5-1) of a segment pipe and plate type heat exchanger (5)
Connect, and between shell and tube exchanger (3) and plate type heat exchanger (5), be provided with a water pump (8) and a dynamic valve, plate type heat exchanger
(5) acid discharge hole (5-3) by a segment pipe with collection acid filling (11) be connected, the outlet (5-2) of plate type heat exchanger (5) with catchment
The first water inlet (4-2) connection of (4) is filled, first outlet (4-1) of filling (4) of catchmenting passes through a segment pipe and steam boiler
(6) connect, catchment and between filling (4) and steam boiler (6), be provided with a water pump (8) and a dynamic valve, catchment the second of filling (4)
Outlet (4-3) is connected with shell and tube exchanger (3) by a segment pipe, is catchmented and is set between filling (4) and shell and tube exchanger (3)
There are a water pump (8) and a dynamic valve, on second outlet (3-3) and flash tank (2) side wall of shell and tube exchanger (3)
Water inlet connects, and the upper end venthole of flash tank (2) is connected with the top air intake of condenser (12), the upper end of condenser (12)
It is connected with injecting type unit (7) lower end by a segment pipe, the lower end of condenser (12) is connected with filling (4) of catchmenting by a segment pipe
Connect, one end of injecting type unit (7) is connected with the venthole of steam boiler (6), the other end and the industry of injecting type unit (7) are given birth to
The air intake connection of workshop (1) is produced, the lower end outlet (2-3) of flash tank (2) passes through the lower end of a segment pipe and filling (4) of catchmenting
Second water inlet (4-4) connects, and flash tank (2) is provided with a water pump (8) and two power with the pipeline catchmented between filling (4)
Valve, two dynamic valves be separately mounted to the flash tank (2) with the pipeline catchmented between filling (4) on.
2. the non-clean Steam Recovery utilization system of a kind of injecting type according to claim 1, it is characterised in that：It is also
Including butterfly valve (9), butterfly valve (9) is connected in parallel on injecting type unit (7) by pipeline.
3. the non-clean Steam Recovery utilization system of a kind of injecting type according to claim 1, it is characterised in that：Steam
Pipeline between boiler (6) and injecting type unit (7) is provided with dynamic valve, temperature sensor and pressure transducer.
4. the non-clean Steam Recovery utilization system of a kind of injecting type according to claim 3, it is characterised in that：Power
Valve is arranged on the pipeline between steam boiler (6) and injecting type unit (7), and temperature sensor is installed in pressure transducer
The steam outlet of steam boiler (6).
5. the non-clean Steam Recovery utilization system of a kind of injecting type according to claim 4, it is characterised in that：Injection
Pipeline between formula unit (7) and commercial production workshop (1) is provided with dynamic valve, temperature sensor and pressure transducer.
6. the non-clean Steam Recovery utilization system of a kind of injecting type according to claim 1, it is characterised in that：Flash distillation
The upper end of tank (2) is provided with temperature sensor and pressure transducer.
7. the non-clean Steam Recovery utilization system of a kind of injecting type according to claim 1, it is characterised in that：Package
Pipeline between formula heat exchanger (3) and plate type heat exchanger (5) is provided with temperature sensor.
8. the non-clean Steam Recovery utilization system of a kind of injecting type according to claim 7, it is characterised in that：Industry
Pipeline between workshop (1) and shell and tube exchanger (3) is provided with temperature sensor.
9. the non-clean Steam Recovery utilization system of a kind of injecting type according to claim 1, it is characterised in that：It is board-like
Temperature sensor is provided with the acid discharge mouth of heat exchanger (5).
10. the non-clean Steam Recovery utilization system of a kind of injecting type according to claim 1, it is characterised in that：It
Also include two fluid level measuring instruments (10), two fluid level measuring instruments (10) are separately mounted to the upper end of flash tank (2) and filling of catchmenting
(4) in middle part of sliding channel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611168958.7A CN106524112A (en) | 2016-12-16 | 2016-12-16 | Jet type uncleanly steam recovery and comprehensive utilization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611168958.7A CN106524112A (en) | 2016-12-16 | 2016-12-16 | Jet type uncleanly steam recovery and comprehensive utilization system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106524112A true CN106524112A (en) | 2017-03-22 |
Family
ID=58340218
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611168958.7A Pending CN106524112A (en) | 2016-12-16 | 2016-12-16 | Jet type uncleanly steam recovery and comprehensive utilization system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106524112A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106677851A (en) * | 2017-03-08 | 2017-05-17 | 华北电力大学（保定） | Adiabatic compressed air energy storage system capable of realizing non-throttling humidification, enthalpy increasing and residual heat elimination |
Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6196163B1 (en) * | 2000-01-19 | 2001-03-06 | Chandrakant S. Shah | Boiler feed water heat energy saver |
| US6470835B1 (en) * | 2000-06-15 | 2002-10-29 | Aqua-Chem, Inc. | Plate-type heat exchanger for exhaust gas heat recovery |
| CN101532722A (en) * | 2009-04-16 | 2009-09-16 | 王爱清 | Dual purpose energy-saving boiler for hot water and steam |
| CN101793390A (en) * | 2010-02-08 | 2010-08-04 | 广东省特种设备检测院顺德分院 | Comprehensive recovery method and system of condensation water and dead steam |
| CN102003699A (en) * | 2010-11-25 | 2011-04-06 | 江苏华伦化工有限公司 | Heat utilization and recovery device for steam boiler |
| CN203215660U (en) * | 2013-05-03 | 2013-09-25 | 青岛亿通达新能源有限公司 | Steam heat energy closed cycling device |
| CN103998381A (en) * | 2011-09-09 | 2014-08-20 | 西尔万资源公司 | Industrial water purification and desalination |
| CN203907582U (en) * | 2014-06-27 | 2014-10-29 | 大连东泰有机废物处理有限公司 | Condensate water recovery system |
| JP2015052406A (en) * | 2013-09-05 | 2015-03-19 | 東京瓦斯株式会社 | Drain recovery equipment, operation method of the same, and heat utilization system using drain recovery equipment |
| CN204611733U (en) * | 2015-03-18 | 2015-09-02 | 四川新华扬山野生物有限公司 | The recycling system of boiler afterheat |
| CN204730179U (en) * | 2015-05-27 | 2015-10-28 | 华东理工大学工程设计研究院有限公司 | A kind of lime set recovery system being provided with secondary steam recycling |
| CN206257647U (en) * | 2016-12-16 | 2017-06-16 | 哈尔滨工大金涛科技股份有限公司 | A kind of non-clean Steam Recovery utilization system of injecting type |
-
2016
- 2016-12-16 CN CN201611168958.7A patent/CN106524112A/en active Pending
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6196163B1 (en) * | 2000-01-19 | 2001-03-06 | Chandrakant S. Shah | Boiler feed water heat energy saver |
| US6470835B1 (en) * | 2000-06-15 | 2002-10-29 | Aqua-Chem, Inc. | Plate-type heat exchanger for exhaust gas heat recovery |
| CN101532722A (en) * | 2009-04-16 | 2009-09-16 | 王爱清 | Dual purpose energy-saving boiler for hot water and steam |
| CN101793390A (en) * | 2010-02-08 | 2010-08-04 | 广东省特种设备检测院顺德分院 | Comprehensive recovery method and system of condensation water and dead steam |
| CN102003699A (en) * | 2010-11-25 | 2011-04-06 | 江苏华伦化工有限公司 | Heat utilization and recovery device for steam boiler |
| CN103998381A (en) * | 2011-09-09 | 2014-08-20 | 西尔万资源公司 | Industrial water purification and desalination |
| CN203215660U (en) * | 2013-05-03 | 2013-09-25 | 青岛亿通达新能源有限公司 | Steam heat energy closed cycling device |
| JP2015052406A (en) * | 2013-09-05 | 2015-03-19 | 東京瓦斯株式会社 | Drain recovery equipment, operation method of the same, and heat utilization system using drain recovery equipment |
| CN203907582U (en) * | 2014-06-27 | 2014-10-29 | 大连东泰有机废物处理有限公司 | Condensate water recovery system |
| CN204611733U (en) * | 2015-03-18 | 2015-09-02 | 四川新华扬山野生物有限公司 | The recycling system of boiler afterheat |
| CN204730179U (en) * | 2015-05-27 | 2015-10-28 | 华东理工大学工程设计研究院有限公司 | A kind of lime set recovery system being provided with secondary steam recycling |
| CN206257647U (en) * | 2016-12-16 | 2017-06-16 | 哈尔滨工大金涛科技股份有限公司 | A kind of non-clean Steam Recovery utilization system of injecting type |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106677851A (en) * | 2017-03-08 | 2017-05-17 | 华北电力大学（保定） | Adiabatic compressed air energy storage system capable of realizing non-throttling humidification, enthalpy increasing and residual heat elimination |
| CN106677851B (en) * | 2017-03-08 | 2018-11-06 | 华北电力大学（保定） | A kind of un-throttled humidification increasing enthalpy eliminates the adiabatic compression air energy storage systems of afterheat |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105299676B (en) | A kind of flue gas moisture waste-heat recovery device based on hollow micro-nano porous ceramic film | |
| CN107218094A (en) | A kind of multiple pressure flashes the device of organic Rankine bottoming cycle cogeneration | |
| CN101955240B (en) | System for desalinating sweater by utilizing low-temperature low-pressure steam generated by smoke waste heat | |
| CN102519032A (en) | Sewage drainage energy-saving flash tank | |
| CN203203020U (en) | Steam waste heat water recycling device for machining paper | |
| CN203549781U (en) | Waste heat deaerator | |
| CN104296554A (en) | Steam condensing type power station steam condenser chamber vacuumizing system | |
| CN106196147A (en) | A kind of exhaust steam residual heat that reclaims improves the thermal efficiency and the system of unit on-load ability | |
| CN206257647U (en) | A kind of non-clean Steam Recovery utilization system of injecting type | |
| CN106524112A (en) | Jet type uncleanly steam recovery and comprehensive utilization system | |
| CN201850152U (en) | System for seawater desalination by utilizing low-temperature and low-pressure steam generated by smoke gas waste heat | |
| CN210241541U (en) | Boiler blow-off water treatment device | |
| CN201373695Y (en) | Combined secondary steam heat energy recovery device for heat pipe phase change heat exchanger of combined heat pump | |
| CN207080982U (en) | A kind of device that can make full use of low-pressure steam heat energy | |
| CN215387651U (en) | Process condensate recovery device of refining device | |
| CN207307226U (en) | A kind of methanol rectification recovery system | |
| CN206874322U (en) | A kind of device of multiple pressure flash distillation organic Rankine bottoming cycle cogeneration | |
| CN201373699Y (en) | Combined secondary steam heat energy recovery device for heat pipe phase change heat exchanger of mechanical compression heat pump | |
| CN209540861U (en) | A kind of condensate liquid step recyclable device | |
| CN102650486B (en) | Closed water cooling system being capable of producing condensed water | |
| CN209431393U (en) | The system of condensed water is recycled in a kind of gas washing in SA production | |
| CN201962221U (en) | Improved alcohol recovering device | |
| CN112274961A (en) | Automatic recovery unit of steam condensate | |
| CN207395510U (en) | A kind of temperature-decreased pressure reducer recycling condensing water device | |
| CN220541798U (en) | Low-pressure exhaust steam and condensed water heat energy efficient utilization system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170322 |