CN201982148U - Vacuum steam heating and pressurizing recovery device for steam turbine - Google Patents
Vacuum steam heating and pressurizing recovery device for steam turbine Download PDFInfo
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- CN201982148U CN201982148U CN2011200193580U CN201120019358U CN201982148U CN 201982148 U CN201982148 U CN 201982148U CN 2011200193580 U CN2011200193580 U CN 2011200193580U CN 201120019358 U CN201120019358 U CN 201120019358U CN 201982148 U CN201982148 U CN 201982148U
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Abstract
The utility model relates to a vacuum steam heating and pressurizing recovery device for a steam turbine which comprises a recycling tank and a jet pump, wherein the recycling tank is provided with a jet pipeline and a water drainage pipeline, a high-pressure pump is arranged on the jet pipeline, a jet outlet of the jet pump is connected with an inlet of the recycling rank through a pipeline, a jet inlet is connected with the jet pipeline, a pumping inlet is connected with a steam discharge pipe of a condenser through a steam inlet pipeline, and the water drainage pipeline is connected with a deoxidization device. By the adoption of the vacuum steam heating and pressurizing recovery device, the vacuum steam and the condensation water formed through the cooling of the condenser are pumped into the recycling tank under the pumping action of the jet pump, and after heated and pressurized in the recycling tank, the condensation water is delivered into the deoxidization device, so that the heat quantity required in heating the condensation water entering the deoxidization device up to the saturated temperature is reduced. Therefore, the recover and reuse of the water resource and heat energy in the vacuum steam are realized, and the purposes of energy conservation and environmental protection are achieved.
Description
Technical field
The utility model relates to a kind of steam turbine vacuum vapour reclamation set, and particularly a kind of steam turbine vacuum stripping temperature pressure-raising reclamation set is used for the recycling of the vacuum vapour of steam turbine discharging.
Background technique
Steam turbine vacuum steam reclamation system of the prior art mainly is that the vapour-water circulation system that adopts steam turbine, vapour condenser, oxygen-eliminating device and cooling tower to constitute realizes the recycling of water resources in the vacuum vapour and the discharging of used heat, though the water resources that adopts this kind vacuum steam reclamation system to reclaim effectively in the vacuum vapour is utilized again, but a large amount of industrial waste heats that carry in the vacuum vapour are discharged in the atmosphere directly or indirectly, have also caused the thermo-pollution of environment when wasting a large amount of heat energy.
The model utility content
For overcoming the above-mentioned defective of prior art, the purpose of this utility model is to provide a kind of steam turbine vacuum stripping temperature pressure-raising reclamation set, can be under the working condition that does not influence vacuum equipment, the water resources in the vacuum vapour and heat energy are carried out recycling behind the temperature raising pressure-raising.
The utility model realizes that the technological scheme that above-mentioned purpose adopted is:
A kind of steam turbine vacuum stripping temperature pressure-raising reclamation set, comprise recycling can and Jet injector, described recycling can is provided with jet pipeline and drainage pipe, described jet pipeline is provided with high-pressure service pump, the jet exit of described Jet injector connects the import of described recycling can by pipeline, jet inlet connects described jet pipeline, and the suction inlet is by the exhaust steam pipe of admission pipeline connection vapour condenser, and described drainage pipe connects described oxygen-eliminating device.
Described steam turbine vacuum stripping temperature pressure-raising reclamation set can also be provided with intake pipe, one end of described intake pipe can connect the outlet pipe of described vapour condenser, the other end can connect jet inlet, suction inlet or the described recycling can of described Jet injector, the other end of described intake pipe can be connected described jet pipeline for the other end of described intake pipe with the Placement of the jet inlet of described Jet injector, can be provided with high-pressure water pump on the outlet pipe of described intake pipe or described vapour condenser; The Placement of the other end of described intake pipe and the suction of described Jet injector inlet can for: the other end of described intake pipe can be connected described admission pipeline or described Jet injector can be provided with the second suction inlet, and the other end of described intake pipe connects the described second suction inlet; The other end of described intake pipe and the Placement of described recycling can be connected the top of described recycling can for the other end of described intake pipe, can be provided with high-pressure water pump on the outlet pipe of described intake pipe or described vapour condenser.
Can be provided with stop valve on the outlet pipe of described vapour condenser, described stop valve can be positioned at the front, joint of the outlet pipe of described intake pipe and vapour condenser.
Described steam turbine vacuum stripping temperature pressure-raising reclamation set can also be provided with the moisturizing pipeline, one end of described moisturizing pipeline can connect the moisturizing source, the other end can connect jet inlet, suction inlet or the described recycling can of described Jet injector, the other end of described moisturizing pipeline can be connected described jet pipeline for the other end of described intake pipe with the Placement of the jet inlet of described Jet injector, can be provided with high-pressure water pump on the described moisturizing pipeline; The other end of described moisturizing pipeline can adopt following arbitrary mode to be connected with the suction of described Jet injector inlet: the other end of described moisturizing pipeline can connect described admission pipeline or described Jet injector can be provided with the 3rd suction inlet, and the other end of described moisturizing pipeline can connect described the 3rd suction inlet; The other end of described moisturizing pipeline and the Placement of described recycling can can be connected the top of described recycling can for the other end of described moisturizing pipeline, can be provided with high-pressure water pump on the described moisturizing pipeline.
Described Jet injector is preferably vertical Jet injector, axially vertically downward, is positioned at the top of described recycling can, and described suction inlet, the second suction inlet and the 3rd suction inlet can be arranged on the axial diverse location of described Jet injector.
Described admission pipeline can be provided with the extension in the pump housing that extends into described Jet injector, described jet pipeline can comprise one-level jet pipe and secondary jets pipe, described one-level jet pipe can penetrate outside the pump housing of described Jet injector in the pump housing of described Jet injector, and be connected with the pump housing of described Jet injector, the part that is communicated with its pump housing that is positioned at described Jet injector with the pump housing of described Jet injector can be extended along the Way out of the extension of pipeline, and the end is provided with the outlet of one-level jet pipe; Described secondary jets pipe can penetrate outside described admission pipeline in the described admission pipeline, and be connected with described admission pipeline, be communicated with described admission pipeline, its be positioned at described admission pipeline part can along described admission pipeline MEDIA FLOW to direction be provided with secondary jets pipe outlet.
Described jet pipeline can also comprise three grades of jet pipes, described three grades of jet pipes can penetrate outside the extension of the pump housing of described Jet injector and described admission pipeline in the extension of the pump housing of described Jet injector and Jet injector admission line, and be connected with the pump housing of described Jet injector and the extension of admission pipeline, be communicated with the extension of described admission pipeline, its be positioned at described admission pipeline the extension part can along the MEDIA FLOW of the extension of described Jet injector admission pipeline to direction extend, the end is provided with three grades of jet pipes outlets.
The bearing of trend of the extension of described admission pipeline can be the direction that flows to along medium in the pump housing of described Jet injector, and the position of described one-level jet pipe outlet can be positioned at the front end of outlet of the extension of described admission pipeline.
The quantity of described recycling can is several, the quantity of described Jet injector is identical with the quantity of described recycling can, and corresponding one by one the setting, the drainage pipe of some described recycling cans can connect described oxygen-eliminating device respectively maybe can connect same main drainpipe road, described main drainpipe road can connect described oxygen-eliminating device, described admission pipeline can be provided with the corresponding one by one some arms that also connect of suction inlet with some described Jet injectors, described intake pipe all can be provided with the some arms identical with the arm quantity of described admission pipeline with the moisturizing pipeline, can connect respectively and they jet inlets of described Jet injector one to one, suction inlet or recycling can.
Described recycling can be provided with safety valve and outlet valve, described safety valve and outlet valve can be connected to the top of described recycling can by pipeline, described water of condensation outlet can be arranged on the bottom of described recycling can, described drainage pipe can be provided with high-pressure service pump and draining pneumatic cut-off valve, high-pressure service pump on described jet pipeline and the drainage pipe all can adopt the parallel way setting of the using and the reserved, described recycling can be provided with the sensing device that is used to gather its water level signal, the signal output part of described sensing device can connect a control gear, and the control signal output terminal of described control gear can connect described draining pneumatic cut-off valve.
The beneficial effects of the utility model are: by Jet injector suction mode the vacuum vapour in the turbine condenser is drawn in the recycling can, and with the jar internal pressure that these exhaust steam form by Jet injector be converted into can reuse steam or high-temperature high pressure water, not only effectively utilized the exhaust steam of steam turbine, and by in vapour condenser, having increased the suction effect of Jet injector, can increase substantially the degree of vacuum in the vapour condenser, thus at the adjust the play that guarantees the normal operation of steam turbine, help reducing required condensing degree of vacuum, reduction is to the cooling requirement of follow-up cooling tower, can reduce the construction cost that cooling tower etc. causes significantly, operating cost and floor space, the water yield and the heat of cooling tower discharging have been reduced significantly, help saving the resource and the energy, also avoided the independent use Jet injector recovery power consumption that exhaust steam in steam turbine brought big simultaneously, the defective of performance difficulty; Owing to the water of condensation in the vapour condenser is introduced Jet injector by intake pipe; and can be by the pressure of original high-pressure service pump formation on the vapour condenser waste pipe; the jet that provides for Jet injector; reduced the power consumption of Jet injector thus; particularly the water of the vacuum vapour of admission pipeline introducing and intake pipe (and water-adding pipe) introducing mixes mutually by Jet injector; be not only vacuum vapour and be condensed into water; and the latent heat of vaporization that discharges can provide the temperature of water in the recycling can significantly; formation has higher temperature (surpassing 90 degree Celsius usually); oxygen-eliminating device is sent in pressurization by the high-pressure service pump on the drainage pipe; can reduce the heat that the water of condensation that enters oxygen-eliminating device is heated to the required absorption of saturation temperature; realize recycling thus to water resources in the vacuum vapour and heat energy; reach the purpose of energy saving and environmental protection, also can bring direct economic benefit simultaneously to enterprise.
Because Jet injector can adopt the mode of multistage jet, make a plurality of zoness of different of Jet injector all owing to jet produces negative pressure being sucked medium or being sucked medium and the mixture of jet media formation suction force its zone of flowing through, make and be sucked medium or be sucked medium and the mixture of jet media this zone of quickening to flow through, form multistage jet, remedy and be sucked medium or be sucked medium and the flow velocity loss of the mixture of jet media in the pipeline or the pump housing, increase substantially the suction capactity and the intake that is sucked medium of Jet injector thus, satisfy more high efficiency medium transport requirement.
Since the Way out of extension, secondary jets pipe and three grades of jet pipes of admission pipeline all be arranged to along MEDIA FLOW in the pump housing to direction, make each jet pipe jet, admission pipeline internal medium flow and the pump housing of described Jet injector in the flow direction of medium identical, do not influence suction force each other, guaranteed the suction effect of Jet injector because of the counteracting of the power of generation.
Owing to adopted vertical Jet injector, and vertical Jet injector is arranged on the top of recycling can, the flow direction of the medium (water or steam water interface) in the Jet injector vertically downward, made full use of the potential energy of water, the kinetic energy that relies on water to form from top to bottom provides the velocity of medium in the Jet injector effectively, improved suction force, can save the required power consumption of jet significantly thus the admission of suction inlet, water inlet.
Description of drawings
Fig. 1 is the utility model first embodiment's an overall structure schematic representation;
Fig. 2 is the utility model second embodiment's an application structure schematic representation.
Embodiment
For clearer explanation the utility model, so that the utility model is more readily understood, the utility model will be further described below in conjunction with accompanying drawing.
Referring to Fig. 1, the utility model provides a kind of steam turbine vacuum stripping temperature pressure-raising reclamation set, can be used with vacuum steam reclamation system or device, comprise recycling can 1 and Jet injector 2, described Jet injector is preferably vertical Jet injector, axially vertically downward, be positioned at the top of described recycling can, described recycling can is provided with jet pipeline 3 that is used to form jet and the drainage pipe 4 that is used for draining, described jet pipeline is provided with high-pressure service pump, be used to improve the pressure of pipeline internal medium, the jet exit of described Jet injector connects the import of described recycling can, the import of described recycling can preferably is arranged on the top of described recycling can, makes jet enter behind the described recycling can stream from the top down, and the import of described recycling can also can be arranged on the side of the body of described recycling can.The jet inlet of described Jet injector connects described jet pipeline, suction inlet by admission pipeline 5 connection vapour condenser 6 or exhaust steam pipe, be used for the vacuum vapour in the described vapour condenser is aspirated into described Jet injector, after mixing, jet media enters described recycling can, realize the recovery of the heat energy of vacuum vapour, described drainage pipe connects oxygen-eliminating device 8, is used for the water of condensation in the described recycling can is flowed to described oxygen-eliminating device.
Preferably adopt effective combination of following dual mode or dual mode about the method for supplementing water of the recycling of the water resources in the vacuum vapour and described recycling can:
One, the water of condensation that will form by vapour condenser cooling and the supplementing water of coming self-water replenishing source 9 are introduced jet inlet, suction inlet or the described recycling can of described Jet injector by pipeline, can also connect the pipeline that jet inlet or suction inlet with described Jet injector connect.For example: described coupling vacuum stripping temperature pressure-raising reclamation set can be provided with intake pipe 11 and moisturizing pipeline 10, one end of described intake pipe can connect the outlet pipe of described vapour condenser, the other end can connect described Jet injector jet pipeline, together enter the jet inlet of Jet injector with the ducted jet media of described jet, in Jet injector, form required jet, for the water of condensation from the outlet pipe of described vapour condenser can successfully be imported in the described jet pipeline, can be provided with high-pressure water pump 12 on the intake pipe between described vapour condenser and the jet pipeline or the outlet pipe of vapour condenser, the discharge pressure of high-pressure water pump is preferably 0.6-1.5MPa, perhaps the other end of described intake pipe can connect described admission pipeline, perhaps the other end of described intake pipe can directly connect described recycling can, for the water of condensation that enters described recycling can is from up to down flowed, the other end of described intake pipe can be connected the top of described recycling can, owing to have certain pressure in the described recycling can, for making water of condensation can enter described recycling can smoothly, can be provided with high-pressure water pump on the described intake pipe between described vapour condenser and the recycling can or the outlet pipe of vapour condenser from the outlet pipe of described vapour condenser; One end of described moisturizing pipeline can connect the moisturizing source usually, the other end can adopt the Placement identical with described intake pipe, when the other end of described moisturizing pipeline connects jet pipeline or recycling can, for making supplementing water can import described jet pipeline or recycling can smoothly from described moisturizing source, can be provided with high-pressure water pump on the described moisturizing pipeline, the discharge pressure of high-pressure water pump is preferably 0.6-1.5MPa.
Two, on described Jet injector, be provided for aspirating the suction inlet of water of condensation that forms by the vapour condenser cooling and the supplementing water of coming the self-water replenishing source, concrete mode is: except that being used to insert the described suction inlet of condenser vacuum vapour, described Jet injector can also be provided with a plurality of other suction inlets, for example the second suction inlet and the 3rd suction enter the mouth, described suction inlet, the second suction inlet and the 3rd suction inlet can be arranged on the axial diverse location of described Jet injector, the described second suction inlet can connect the outlet pipe of described vapour condenser by intake pipe, be used for the water of condensation of the outlet pipe of described vapour condenser is aspirated into described Jet injector and then entered described recycling can, described the 3rd suction inlet can connect described moisturizing source by the moisturizing pipeline, is used for aspirating as described Jet injector from the supplementing water in described moisturizing source and then entering described recycling can.
In actual applications, the outlet pipe of described vapour condenser connects described oxygen-eliminating device usually, at this moment, described drainage pipe can connect the outlet pipe of described vapour condenser, the joint is arranged in the front, joint of outlet pipe and described intake pipe of described vapour condenser, and (the application's front and rear direction defines according to the media flow direction of corresponding pipeline, down together), can be provided with stop valve on the outlet pipe of the described vapour condenser between two joints, with the whereabouts of the medium in the outlet pipe of the described vapour condenser of convenient control.
The utility model can aspirate into described recycling can by the pumping action of described Jet injector with vacuum vapour and by the water of condensation that described vapour condenser cooling back forms; rely on the pressure of described Jet injector in described recycling can, to form high pressure; vacuum vapour forms water of condensation under the high pressure effect; volume reduces; guaranteed the degree of vacuum of vacuum equipment; and water of condensation temperature and pressure in described recycling can raises; part water of condensation forms jet by described jet condensate pump; come back in the described recycling can by described Jet injector; another part water of condensation is delivered to described oxygen-eliminating device by described drainage pipe; realize recycling thus to water resources in the vacuum vapour and heat energy; water of condensation behind the temperature raising pressure-raising is sent into described oxygen-eliminating device; can also reduce the heat that the water of condensation that enters oxygen-eliminating device is heated to the required absorption of saturation temperature, reach the purpose of energy saving and environmental protection.
The preferred multi-stage multi-pipe jet injector with high efficiency of described Jet injector, described admission pipeline can be provided with the extension in the pump housing that extends into described Jet injector, described jet pipeline can comprise the one-level jet pipe, secondary jets pipe and three grades of jet pipes, described one-level jet pipe can penetrate outside the pump housing of described Jet injector in the pump housing of described Jet injector, and be connected with the pump housing of described Jet injector, be communicated with the pump housing of described Jet injector, its part that is positioned at the pump housing of described Jet injector can be extended along the Way out of the extension of pipeline, the end is provided with the outlet of one-level jet pipe, be used in the pump housing of described Jet injector, forming first order jet, the MEDIA FLOW of described one-level jet pipe outlet in the described pump housing is to direction, described one-level jet pipe is positioned at the external diameter of part of the pump housing of described Jet injector should be less than the internal diameter of the described pump housing, leave and be sucked the passage that medium passes through, the outlet of described one-level jet pipe also can be arranged to conical outlet, so that form jet better; Described secondary jets pipe can penetrate outside described admission pipeline in the described admission pipeline, and be connected with described admission pipeline, be communicated with described admission pipeline, its be positioned at described admission pipeline part can along described admission pipeline MEDIA FLOW to direction be provided with secondary jets pipe outlet, be used in described admission pipeline, forming second level jet, the MEDIA FLOW of described secondary jets pipe outlet in described admission pipeline be to direction, and the external diameter that described secondary jets pipe is positioned at the part of described admission pipeline should leave less than the internal diameter of described admission pipeline and be sucked the passage that medium passes through; Described three grades of jet pipes can penetrate outside the extension of the pump housing of described Jet injector and described admission pipeline in the extension of the pump housing of described Jet injector and Jet injector admission line, and be connected with the pump housing of described Jet injector and the extension of admission pipeline, be communicated with the extension of described Jet injector admission line, its be positioned at described admission pipeline the extension part can along the MEDIA FLOW of the extension of described Jet injector admission pipeline to direction extend, the end is provided with three grades of jet pipe outlets, be used in the extension of described admission pipeline, forming third level jet, described three grades of jet pipes outlet in the extension of described admission pipeline MEDIA FLOW to direction, described three grades of jet pipes are positioned at the external diameter of part of the extension of described Jet injector admission line should be less than the internal diameter of the extension of described admission pipeline, leave and be sucked the passage that medium passes through, described three grades of jet pipes outlet can be arranged to conical outlet, so that form jet better.
In order to improve the suction effect of second level jet, the part that described secondary jets pipe is positioned at described admission pipeline can be provided with the secondary jets pipe extension of extending along described admission pipeline radial direction, the end sealing of described secondary jets pipe extension, the quantity of described secondary jets pipe outlet can be several, can evenly be arranged on the described secondary jets pipe extension, further, described secondary jets pipe extension can be provided with the cross pipe that one or several intersect and be communicated with it along described suction pipe radial direction, the closed at both ends of described cross pipe, several described secondary jets pipe outlets can evenly be arranged on described secondary jets pipe extension and the cross pipe, a preferred cross pipe and the described secondary jets pipe extension of adopting is the decussation ways of connecting, guaranteeing second level jet location jet media pressure everywhere like this, flow velocity and in its back-end because under the prerequisite of the negative pressure basis equalization that jet produces, can in described suction pipe, leave the medium channel of larger sectional area again, be convenient to be sucked passing through of medium, adopt this kind set-up mode to help reducing turbulent flow and resistance, and improve suction force that is sucked medium and the mixing efficiency that is sucked medium and jet media.
MEDIA FLOW can evenly be provided with several injection pipes to direction in the described suction pipe in described secondary jets pipe extension and cross pipe upper edge, the jetburner of described injection pipe is described secondary jets pipe outlet, the ratio of the internal diameter of described injection pipe and described admission pipeline is not more than 1: 5, the ratio of the internal diameter of the diameter of preferred described injection pipe and described admission pipeline is not more than 1: 10, as 1: 10,1: 12,1: 15,1: 18,1: 20 or 1: 30, to improve the flow velocity of second level jet, thereby improve suction force and to being sucked the suction effect of medium, described secondary jets pipe outlet can be arranged to conical outlet, so that form jet better.
The bearing of trend of the extension of described admission pipeline can be the direction that flows to along medium in the pump housing of described Jet injector, adopt this kind setting, help improving the jet effect of described three grades of jet pipes in described admission pipeline extension, and can be directly the mixture that is sucked medium and jet media that forms being sprayed the into described pump housing behind jet for the third time, convenient described one-level jet pipe aspirates once more to it.The position of described one-level jet pipe outlet can be positioned at the front end of outlet of the extension of described admission pipeline, so that the outlet of the extension of described admission pipeline is positioned at the negative pressure region that described one-level jet pipe jet forms, reach from the better suction effect of medium in the described honeycomb duct extension.
Described one-level jet pipe, secondary jets pipe and three grades of jet pipes can be connected the water of condensation outlet of described recycling can respectively, maybe can connect same jet pipe, and described jet pipe connects the water of condensation outlet of described recycling can.
The quantity of described one-level jet pipe and three grades of jet pipes all can be several, and quantity can be identical, and adopting one to one, relation evenly is arranged on the pump housing of described Jet injector; Quantity also can be different, evenly are arranged on the pump housing of described Jet injector respectively.
Reference is to the setting of the multistage jet of described admission pipeline, and described intake pipe and moisturizing pipeline also can be arranged to the form of multistage jet.
Described Jet injector adopts the mode of multistage jet, make a plurality of zoness of different of described Jet injector all owing to jet produces negative pressure being sucked medium or being sucked medium and the mixture of jet media formation suction force its zone of flowing through, make and be sucked medium or be sucked medium and the mixture of jet media this zone of quickening to flow through, form multistage jet, remedy and be sucked medium or be sucked medium and the flow velocity loss of the mixture of jet media in the pipeline or the pump housing, increase substantially the suction capactity and the intake that is sucked medium of Jet injector thus, satisfy more high efficiency medium transport requirement.
The Way out of the extension of described admission pipeline, one-level jet pipe and three grades of jet pipes all be arranged to along MEDIA FLOW in the pump housing to direction, make each jet pipe jet, admission pipeline internal medium flow and the pump housing of described Jet injector in the flow direction of medium identical, do not influence suction force each other, guaranteed the suction effect of Jet injector because of the counteracting of the power of generation.
According to different real work situations, discharge capacity as steam turbine vacuum vapour is bigger, the quantity of described recycling can be arranged to several, the quantity of described Jet injector is identical with the quantity of described recycling can, and corresponding one by one the setting, adopt mode in parallel jointly the water resources and the heat energy of vacuum vapour to be carried out recycling.The drainage pipe of some described recycling cans can connect the outlet pipe of described oxygen-eliminating device or vapour condenser respectively, also can connect same main drainpipe road, described main drainpipe road connects the outlet pipe of described oxygen-eliminating device or vapour condenser, when adopting this kind to be provided with, described admission pipeline, Jet injector intake pipe and moisturizing pipeline all can be provided with the arm identical with the quantity of described recycling can or Jet injector, and are connected with each self-corresponding Jet injector or pipeline.As: as described in the admission pipeline be provided with some as described in some arms of the corresponding one by one and connection of the suction inlet of Jet injector, described intake pipe is equipped with the some arms identical with the arm quantity of described admission pipeline with the moisturizing pipeline, connects respectively and the arm of their described one to one admission pipelines or the jet pipeline of described recycling can; Perhaps described admission pipeline, Jet injector intake pipe and moisturizing pipeline are equipped with respectively and aspirate some arms that inlet is corresponding one by one and be connected with suction inlet, the second suction inlet and the 3rd of some described Jet injectors.
Described recycling can be provided with safety valve and outlet valve, described safety valve and outlet valve can be connected to the top of described recycling can by pipeline, the gas that can not form water of condensation regularly can be discharged by described outlet valve, in order to avoid take the space of described recycling can too much, described safety valve can be in described recycling can internal pressure above releasing pressure automatically after the certain limit.May have water of condensation, steam and incoagulable gas simultaneously in the described recycling can, steam and water of condensation form transient equiliblium under certain pressure and water of condensation discharge amount.Described water of condensation outlet can be arranged on the bottom of described recycling can, what guarantee thus to export out from described water of condensation all is water of condensation, described drainage pipe can be provided with draining condensate pump and draining pneumatic cut-off valve 13, described jet condensate pump and draining condensate pump all can adopt the parallel way setting of the using and the reserved, should require to select for use suitable water pump as jet condensate pump and draining condensate pump according to temperature, flow and pressure.Described jet condensate pump and draining condensate pump can require according to the jet pressure of described Jet injector and the pressure of drainage system requires selected pump pressure, described recycling can be provided with the sensing device 14 that is used to gather its water level signal, the signal output of described sensing device can connect a control gear, described control gear can be according to default program or Control Parameter work, its control signal output can connect described draining pneumatic cut-off valve by circuit, so that draining is controlled according to the water level in the described recycling can, the water level in the described recycling can is maintained in certain scope.
Referring to Fig. 2, when the employing of steam turbine vacuum steam reclamation system is provided with the form of gland heater 15 and multistage heater 16 in the water of condensation outlet rear end of vapour condenser, described intake pipe can be connected on the intake pipe of a heater in the described multistage heater, can be provided with stop valve on the intake pipe between joint and this heater, the whereabouts that is used for control media, described drainage pipe can connect the outlet pipe of this heater, is used for sending the water of condensation behind the temperature raising pressure-raising back to original system.
All can be provided with suitable valve on related each pipeline of the utility model, realize control with convenient.
The diameter of each pipeline that the utility model is related can be according to the size and the suitable selection of requirement of engineering of Jet injector and recycling can, described each pipeline can adopt isometrical pipe, with convenient processing, can at least one be not isometrical pipe also, with flow velocity and the resistance requirement that adapts to diverse location.Can adopt the mode of welding, single injection-molded or other any suitable to be connected between described each pipeline and between each pipeline and the described Jet injector, arbitrary body passes the interconnecting to be and be tightly connected of the pump housing of another body or Jet injector.
Claims (10)
1. steam turbine vacuum stripping temperature pressure-raising reclamation set, it is characterized in that comprising recycling can and Jet injector, described recycling can is provided with jet pipeline and drainage pipe, described jet pipeline is provided with high-pressure service pump, the jet exit of described Jet injector connects the import of described recycling can, jet inlet connects described jet pipeline, and the suction inlet is by the exhaust steam pipe of admission pipeline connection vapour condenser, and described drainage pipe connects described oxygen-eliminating device.
2. steam turbine vacuum stripping temperature pressure-raising reclamation set as claimed in claim 1, it is characterized in that also being provided with intake pipe, one end of described intake pipe connects the outlet pipe of described vapour condenser, the other end connects jet inlet, suction inlet or the described recycling can of described Jet injector, the other end of described intake pipe and the Placement of the jet inlet of described Jet injector are that the other end of described intake pipe is connected described jet pipeline, and the outlet pipe of described intake pipe or described vapour condenser is provided with high-pressure water pump; The other end of described intake pipe with the Placement of the suction of described Jet injector inlet is: the other end of described intake pipe is connected described admission pipeline or described Jet injector is provided with the second suction inlet, and the other end of described intake pipe connects the described second suction inlet; The other end of described intake pipe and the Placement of described recycling can are the top that the other end of described intake pipe is connected described recycling can, and the outlet pipe of described intake pipe or described vapour condenser is provided with high-pressure water pump.
3. steam turbine vacuum stripping temperature pressure-raising reclamation set as claimed in claim 2 is characterized in that the outlet pipe of described vapour condenser is provided with stop valve, and described stop valve is positioned at the front, joint of the outlet pipe of described intake pipe and vapour condenser.
4. steam turbine vacuum stripping temperature pressure-raising reclamation set as claimed in claim 3, it is characterized in that it also is provided with the moisturizing pipeline, one end of described moisturizing pipeline connects the moisturizing source, the other end connects jet inlet, suction inlet or the described recycling can of described Jet injector, the other end of described moisturizing pipeline and the Placement of the jet inlet of described Jet injector are that the other end of described intake pipe is connected described jet pipeline, and described moisturizing pipeline is provided with high-pressure water pump; The other end of described moisturizing pipeline adopts following arbitrary mode to be connected with the suction of described Jet injector inlet: the other end of described moisturizing pipeline connects described admission pipeline or described Jet injector is provided with the 3rd suction inlet, and the other end of described moisturizing pipeline connects described the 3rd suction inlet; The other end of described moisturizing pipeline and the Placement of described recycling can are the top that the other end of described moisturizing pipeline is connected described recycling can, and described moisturizing pipeline is provided with high-pressure water pump.
5. steam turbine vacuum stripping temperature pressure-raising reclamation set as claimed in claim 4, it is characterized in that described Jet injector is vertical Jet injector, axially vertically downward, be positioned at the top of described recycling can, described suction inlet, the second suction inlet and the 3rd suction inlet are arranged on the axial diverse location of described Jet injector.
6. as claim 1,2,3,4 or 5 described steam turbine vacuum stripping temperature pressure-raising reclamation sets, it is characterized in that described admission pipeline is provided with the extension in the pump housing that extends into described Jet injector, described jet pipeline comprises one-level jet pipeline and secondary jets pipeline, described one-level jet pipe penetrates in the pump housing of described Jet injector outside the pump housing of described Jet injector, and be connected with the pump housing of described Jet injector, be communicated with the pump housing of described Jet injector, its part that is positioned at the pump housing of described Jet injector is extended along the Way out of the extension of described admission pipeline, and the end is provided with the outlet of one-level jet pipe; Described secondary jets pipe penetrates in the described admission pipeline outside described admission pipeline, and be connected with described admission pipeline, be communicated with described admission pipeline, its part that is positioned at described admission pipeline along described admission pipeline MEDIA FLOW to direction be provided with the outlet of secondary jets pipe.
7. steam turbine vacuum stripping temperature pressure-raising reclamation set as claimed in claim 6, it is characterized in that described jet pipeline also comprises three grades of jet pipelines, described three grades of jet pipes penetrate outside the extension of the pump housing of described Jet injector and described admission pipeline in the extension of the pump housing of described Jet injector and Jet injector admission line, and be connected with the pump housing of described Jet injector and the extension of admission pipeline, be communicated with the extension of described admission pipeline, its be positioned at described admission pipeline the extension part along the MEDIA FLOW of the extension of described Jet injector admission pipeline to direction extend, the end is provided with three grades of jet pipes outlets.
8. steam turbine vacuum stripping temperature pressure-raising reclamation set as claimed in claim 7, the bearing of trend of extension that it is characterized in that described admission pipeline is for along the direction that flows to of medium in the pump housing of described Jet injector, and the position of described one-level jet pipe outlet is positioned at the front end of outlet of the extension of described admission pipeline.
9. steam turbine vacuum stripping temperature pressure-raising reclamation set as claimed in claim 8, the quantity that it is characterized in that described recycling can is several, the quantity of described Jet injector is identical with the quantity of described recycling can, and with one one corresponding setting, the drainage pipe of some described recycling cans connects described oxygen-eliminating device respectively or connects same main drainpipe road, described main drainpipe road connects described oxygen-eliminating device, described admission pipeline is provided with the corresponding one by one some arms that also connect of suction inlet with some described Jet injectors, described intake pipe is equipped with the some arms identical with the arm quantity of described admission pipeline with the moisturizing pipeline, connects respectively and they jet inlets of described Jet injector one to one, suction inlet or recycling can.
10. steam turbine vacuum stripping temperature pressure-raising reclamation set as claimed in claim 9, it is characterized in that described recycling can is provided with safety valve and outlet valve, described safety valve and outlet valve are connected to the top of described recycling can by pipeline, described water of condensation outlet is arranged on the bottom of described recycling can, described drainage pipe is provided with high-pressure service pump and draining pneumatic cut-off valve, high-pressure service pump on described jet pipeline and the drainage pipe all adopts the parallel way setting of the using and the reserved, described recycling can is provided with the sensing device that is used to gather its water level signal, the signal output part of described sensing device connects a control gear, and the control signal output terminal of described control gear connects described draining pneumatic cut-off valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200193580U CN201982148U (en) | 2011-01-21 | 2011-01-21 | Vacuum steam heating and pressurizing recovery device for steam turbine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200193580U CN201982148U (en) | 2011-01-21 | 2011-01-21 | Vacuum steam heating and pressurizing recovery device for steam turbine |
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| Publication Number | Publication Date |
|---|---|
| CN201982148U true CN201982148U (en) | 2011-09-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200193580U Expired - Fee Related CN201982148U (en) | 2011-01-21 | 2011-01-21 | Vacuum steam heating and pressurizing recovery device for steam turbine |
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| CN (1) | CN201982148U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102108886A (en) * | 2011-01-21 | 2011-06-29 | 李树生 | Vacuum steam heating and pressurizing recycling device for steam turbine |
| CN103267425A (en) * | 2013-05-30 | 2013-08-28 | 深圳市广前电力有限公司 | Method and device for solving condenser low vacuum in combined cycle unit starting process |
-
2011
- 2011-01-21 CN CN2011200193580U patent/CN201982148U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102108886A (en) * | 2011-01-21 | 2011-06-29 | 李树生 | Vacuum steam heating and pressurizing recycling device for steam turbine |
| CN103267425A (en) * | 2013-05-30 | 2013-08-28 | 深圳市广前电力有限公司 | Method and device for solving condenser low vacuum in combined cycle unit starting process |
| CN103267425B (en) * | 2013-05-30 | 2015-05-13 | 深圳市广前电力有限公司 | Method and device for solving condenser low vacuum in combined cycle unit starting process |
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Granted publication date: 20110921 Termination date: 20140121 |