CN103480193A - Precision treater for condensed water - Google Patents

Precision treater for condensed water Download PDF

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Publication number
CN103480193A
CN103480193A CN201310448040.8A CN201310448040A CN103480193A CN 103480193 A CN103480193 A CN 103480193A CN 201310448040 A CN201310448040 A CN 201310448040A CN 103480193 A CN103480193 A CN 103480193A
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China
Prior art keywords
backwash
cavity
cylindrical shell
shaft coupling
resorption
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CN201310448040.8A
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CN103480193B (en
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俞蓉
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CHANGSHU HUANENG WATER-TREATING EQUIPMENT Co Ltd
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CHANGSHU HUANENG WATER-TREATING EQUIPMENT Co Ltd
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Abstract

A precision treater for condensed water belongs to the technical field of water treatment equipment, and comprises a barrel, a barrel cavity partition plate, a group of lower cavity filter elements, a condensed water leading-in pipe, a spacer sleeve, a return water pipe, a back-wash pipe drive mechanism and a back-wash pipe, wherein the barrel is provided with an upper seal head and a lower seal head; the barrel cavity partition plate is arranged in a barrel cavity; a group of lower cavity filter element liquid outlet matching holes are formed in the barrel cavity partition plate; the lower cavity filter elements are arranged in the lower cavity of the barrel; the condensed water leading-in pipe is fixed with the bottom of the lower seal head; the spacer sleeve is fixed on one side of the upper seal head; a spacer sleeve water inlet connector extends from one side of the spacer sleeve; a one-way valve is arranged on the water inlet connector; one end of the return water pipe extends into the cavity of the spacer sleeve, and the other end thereof extends out of the barrel cavity; the back-wash pipe drive mechanism is arranged on the upper seal head; the upper end of the back-wash pipe extends into the cavity of the spacer sleeve, and the lower end thereof is supported in the center of the barrel cavity partition plate. The precision treater has the characteristics that a back-wash liquid spray arm is fixed at the lower end of the back-wash pipe, a spray arm opening is formed in the bottom of the back-wash liquid spray arm, the back-wash effect is ideal, the back-wash time is shortened, energy is saved, the outage time of the equipment is shortened, the structure is simplified, and the material is saved.

Description

The condensate fine processor
Technical field
The invention belongs to the water treatment facilities technical field, be specifically related to a kind of condensate fine processor, the processing of the steam technique condensate water produced for the industry to such as petrochemical industry, oil refining industry, biology,drug and chemical industry industry, power station and papermaking.
Background technology
Above mentioned condensate water also claims condensate liquid or surface condensate and even is called the technique condensate water, and accordingly, above mentioned condensate fine processor also can be described as the condensate liquid polisher.Take chemical industry and oil refining industry as example, need in process of production to use in large quantities high-temperature steam as the energy to various oil product heating, steam is converted into condensate water after heat exchange, from gaseous state, becomes liquid state.If using condensate water as discharge of wastewater, can cause valuable water resource waste so; Passed through again desalting processing before due to this condensate water, once therefore discarded, certainly can increase unreasonably the water cost; Also owing to often being attended by micro-hydrocarbons and wet goods etc. in condensate water, therefore directly discharge can undermine environment, and if qualified discharge after treatment, although can avoid affecting environment, cost of water treatment is higher.Condensate water is used as boiler feedwater; but but not only saving water resource but also protection of the environment; but; due to the oil content in condensate water about about 1-200ml/L; contain oil standard higher than boiler feedwater far away; thereby can not be using condensate water directly as boiler feedwater, otherwise the working life of boiler can be seriously undermined, and the purity of the steam that boiler produces can be had a strong impact on.
Utilize the condensate water preprocessor to the condensate water pretreatment; and filter through active carbon filter; and, by the precision processing of condensate fine processor, finally as boiler feedwater up to standard, be back to that boiler can be received saving water resource, protection of the environment, the effect of the many carvings of an arrow that reduce production costs.Because can be by the hydrocarbons in condensate water the impurity filterings such as hydrocarbon compound (alkane, cycloalkane, alkene, alkynes and aromatic hydrocarbon), oil, iron oxide after pretreatment, activated carbon filtration and precision processing.The complete treatment system consisted of condensate water preprocessor, active carbon filter and condensate fine processor is called condensate polishing system, can refer to " process condensed water processing system (this patent is proposed by the applicant) " that Chinese invention patent Granted publication CN102091480B recommends to this.
No matter be condensate water preprocessor or condensate fine processor, be provided with filter core in cylindrical shell, by filter core to impurity filterings such as the aforementioned greasy dirt in condensate water, hydrocarbon compound, iron oxide, and after condensate water is processed to a period of time, the cause of being stopped up due to filter core, the pressure reduction of condensate water turnover cylindrical shell increases, when reaching while being about 0.15MPa, pressure reduction need to carry out backwash to filter core, to reduce pressure reduction, that is to say and make pressure reduction be restored to normal pressure difference, to ensure filter efficiency and the filter effect to condensate water.
Water consumption while in order to reduce, the filter core in the cylindrical shell of condensate fine processor being implemented to backwash and guarantee backwash effect, therefore, usually the condensate fine processor is equipped with to a backwash mechanism, " filter " (this patent is proposed by the applicant) confirmation that the condensate fine processor of this structure can be provided by invention patent mandate notification number CN100488594C.
The technical scheme that aforementioned CN100488594C provides is owing to being separated out one group of backwash synergy chamber independently separately on the cylindrical shell dividing plate, so when implementing backwash, become and concentrate on certain backwash synergy chamber originally sharing counter-flushing liquid in whole cylindrical shell epicoele equally, flow velocity in unit interval is doubled, for example, when backwash synergy chamber is separated into eight independently zones or while claiming chamber, flow velocity in unit interval has increased octuple so, the counter-flushing liquid of originally sharing eight zones concentrates on a zone, thereby be able to the mistake filter core corresponding to this below, zone effectively clean, made filter core obtain the service life (specifically can refer to the 7th page of the 2nd section explanation to the 8th page of the 6th row of specification of this patent) of desirable backwash cleaning effect and prolongation filter core, water consumption in the time of can saving backwash simultaneously.
Yet, there is following shortcoming in the backwash mechanism that above-mentioned " filter " is equipped with: one, because the counter-flushing liquid that goes out the self counter flushing liquid outlet was ejected into certain chamber of backwash synergy chamber before this to be tending towards level, then by chamber, make counter-flushing liquid implement backwash in the mode of trickling to the filter core that is positioned at the chamber below downwards, thereby the backwash liquid outlet can not directly be aimed at filter core performance backwash effect, that is to say because counter-flushing liquid does not produce direct jet-action to filter core, so cleaning performance shortcoming to the dirt that attaches on filter core, scavenging period is grown and is wasted water source and affect the time that filter recovers the initialization state, its two, because backwashing time is long, thereby be unfavorable for save supporting the power consumption of the motor of backwash mechanism work, they are three years old, the structure relative complex of backwash synergy chamber, for example need on the dividing plate of cylinder chamber, with the interval state, one component dividing plate be set, organize the demarcation strip distributed radially and form a plurality of backwash synergy chamber by means of the sealing of cover plate on the dividing plate of cylinder chamber by this, therefore not only make trouble, and raw-material use amount is large.
In view of above-mentioned prior art, be necessary then to improve, the applicant has done long-term and useful design for this reason, finally formed technical scheme described below, and taking the laboratory the applicant under the secrecy provision to carry out simulated test, Bearing performance has gone out unexpected technique effect.
Summary of the invention
Task of the present invention is to provide a kind of and contributes to make counter-flushing liquid to aim at filter core directly to spray and use the backwash effect that improves filter core, be conducive to shorten backwashing time and use the water consumption of saving backwash and save power consumption and shorten equipment idle time and be of value to simplified structure and use the convenient condensate fine processor of manufacturing and saving raw and auxiliary material.
Task of the present invention completes like this, and a kind of condensate fine processor comprises that top forms and upper cover to be arranged and bottom forms the cylindrical shell that low head is arranged, a chamber demarcation strip, this chamber demarcation strip is arranged in the cylinder chamber of cylindrical shell and by this chamber demarcation strip, the cylinder chamber of cylindrical shell is divided into to cylindrical shell epicoele and cylindrical shell cavity of resorption with level, on this chamber demarcation strip, with the interval state, offer one group of cavity of resorption filter core liquid outlet mating holes, one group of cavity of resorption filter core, the quantity of this group of cavity of resorption filter core equates with the quantity of described cavity of resorption filter core liquid outlet mating holes, and in the position corresponding to cavity of resorption filter core liquid outlet mating holes, with vertical state, be arranged in described cylindrical shell cavity of resorption, the cavity of resorption filter core liquid outlet of each cavity of resorption filter core matches with cavity of resorption filter core liquid outlet mating holes, one introduces for the condensate water that will await the essence filtration condensate water inlet tube that supplies described cavity of resorption filter element filtering in described cylindrical shell cavity of resorption, and the bottom of this condensate water inlet tube and described low head is fixed, and communicates with the cylindrical shell cavity of resorption, one spacer cylinder and a return pipe, the spacer cylinder is fixed on described upper cover towards a side of described cylindrical shell epicoele and corresponding to the middle position of upper cover, a side of spacer cylinder be extended with one with the spacer cylinder chamber of spacer cylinder, communicate introduce the spacer cylinder water inlet interface in spacer cylinder chamber for the water by the cylindrical shell epicoele, be provided with a check valve on this spacer cylinder water inlet interface, one end of return pipe is in described upper cover is stretched over described cylindrical shell epicoele, be connected with described spacer cylinder and communicate with described spacer cylinder chamber, the other end of return pipe is stretched over outside cylinder chamber, one backwash tube driving mechanism and a backwash tube, the backwash tube driving mechanism is arranged on described upper cover, and corresponding with described spacer cylinder, the upper end of backwash tube is stretched in described spacer cylinder chamber, and be in transmission connection with the backwash tube driving mechanism, and the lower end of backwash tube is bearing in the middle position of described cylinder chamber demarcation strip rotationally, and the sidepiece in the lower end of this backwash tube offers a backwash tube liquid outlet, be characterised in that: in the lower end of described backwash tube and be fixed with a counter-flushing liquid spray arm in the position corresponding to described backwash tube liquid outlet with the horizontal boom state, this counter-flushing liquid spray arm is corresponding to the top of described cylinder chamber demarcation strip, and form a spray arm opening is arranged in the bottom of the length direction of this counter-flushing liquid spray arm, this spray arm opening communicates with the counter-flushing liquid spray arm chamber of counter-flushing liquid spray arm, and counter-flushing liquid spray arm chamber communicates with the backwash tube liquid outlet.
In a specific embodiment of the present invention, form cylindrical shell cavity of resorption inspection mouth is arranged on the sidewall of described cylindrical shell and in the position corresponding to described cylindrical shell cavity of resorption, on this cylindrical shell cavity of resorption inspection mouth, sealing is equipped with a cylindrical shell cavity of resorption inspection lid; Form a cylindrical shell epicoele man-hole opening is arranged on described upper cover, on this cylindrical shell epicoele man-hole opening, sealing is equipped with a manhole lid, and be equipped with a greasy dirt and draw interface on upper cover, this greasy dirt is drawn interface and is communicated with the cylindrical shell epicoele, and draws on interface and be connected with a greasy dirt fairlead at this greasy dirt; Be fixed with one group of cylinder bearing pin on described low head.
In another specific embodiment of the present invention, be equipped with a blowdown interface on the pipeline of described condensate water inlet tube.
In another specific embodiment of the present invention, be equipped with a compressed air at the described other end of described return pipe and introduce interface, a positive flushing water water inlet interface, a water outlet mouthpiece and backwashing water introducing interface.
In another specific embodiment of the present invention, described backwash tube driving mechanism comprises the backwash motor, the backwash reductor, shaft coupling, backwash reductor supporting base, main shaft, signal panels and signal pickup assembly, the backwash motor is connected with the backwash speed reducer drive, and be fixed on backwash reductor supporting base together with the backwash motor by the backwash reductor, and backwash reductor supporting base is fixed on described upper cover, and be positioned at the middle position of upper cover, shaft coupling is connected between the backwash speed reducer output shaft and main shaft of backwash reductor, main shaft is stretched in the spacer cylinder chamber of described spacer cylinder and is in transmission connection with described backwash tube, signal panels are nested with on main shaft, and fix with shaft coupling, offer one group of telltale hole with the equidistant intervals state on these signal panels and around the circumferencial direction of signal panels, signal pickup assembly is fixed on backwash reductor supporting base, and corresponding with described telltale hole, this signal pickup assembly is connected with the electric control box electrical control by circuit, and described backwash motor is connected with the electric control box electrical control equally.
Also has a specific embodiment of the present invention, described shaft coupling comprises, lower shaft coupling and one group of shaft coupling attachment screw, upper shaft coupling and described backwash speed reducer output shaft key are connected and fixed, and should towards an end formation of lower shaft coupling, shaft coupling terminal pad on be arranged by upper shaft coupling, lower shaft coupling and described main shaft key are connected and fixed, and this time shaft coupling has shaft coupling terminal pad towards an end formation of upper shaft coupling, on, lower shaft coupling terminal pad is fitted to each other, one group of shaft coupling attachment screw is with the interval distributions and by upper, lower shaft coupling terminal pad is fixed together, described signal panels and described lower shaft coupling are fixed, be equipped with the logical liquid joint of a backwash tube in the upper end of described backwash tube, the upper end of the logical liquid joint of this backwash tube is positioned at described spacer cylinder chamber, with described main shaft, be fixedly connected with, and offer fluid-through tube joint liquid-through hole with the interval state on the wall body of the upper end of the logical liquid joint of this backwash tube, fluid-through tube joint liquid-through hole communicates with spacer cylinder chamber, the lower end of the logical liquid joint of backwash tube is stretched over outside spacer cylinder chamber and with backwash tube and is fixedly connected with.
More of the present invention and in specific embodiment, described signal pickup assembly comprises signal picker support and signal picker, the signal picker support is fixed on described backwash reductor supporting base, signal picker is fixed on the signal picker support, and be positioned at described signal panels below corresponding with described telltale hole, this signal picker is connected with described electric control box electrical control by the signal picker circuit.
In of the present invention and then specific embodiment, offer one group of adjustment tank with the interval state on described signal panels and in the position corresponding to described lower shaft coupling, respectively be equipped with an adjustment tank attachment screw in the position corresponding to each adjustment tank, each adjustment tank attachment screw and described lower shaft coupling are fixed towards an end end face of signal panels, and described adjustment tank is arc-shaped slot.
Of the present invention again more and, in specific embodiment, described signal picker is photoelectric sensor.
In again of the present invention and then specific embodiment, the diameter of described counter-flushing liquid spray arm diminishes towards the direction away from the backwash tube liquid outlet gradually from described backwash tube liquid outlet, and the radius of the length of counter-flushing liquid spray arm and described cylinder chamber demarcation strip adapts, wherein: a side of the length direction of counter-flushing liquid spray arm and opposite side and be positioned at the counter-flushing liquid spray arm bottom each form a liquid outlet sealing block wing for described cavity of resorption filter core liquid outlet is covered that leans out the lateral surface of counter-flushing liquid spray arm arranged, liquid outlet sealing block wing contacts with described cylinder chamber demarcation strip.
One of technique effect of technical scheme provided by the invention, when backwash, driving backwash tube by the backwash tube driving mechanism rotates, drive and be fixed in counter-flushing liquid spray arm rotation its below and corresponding with the backwash tube liquid outlet by backwash tube, the counter-flushing liquid that comes from the backwash tube liquid outlet enters counter-flushing liquid spray arm chamber and is directly sprayed by the cavity of resorption filter core liquid outlet that the spray arm opening is aimed at the cavity of resorption filter core, thereby can play the desirable backwash effect to the cavity of resorption filter core; Two, because the spray arm opening is right against the top of cavity of resorption filter core liquid outlet, thereby can make current under good pressure state, the cavity of resorption filter-core back-flushing be washed, be conducive to significantly to shorten backwashing time with water consumption, the electric energy of saving backwash and shorten equipment idle time; Three, owing to without resembling prior art, building one group of backwash synergy chamber on the demarcation strip of cylinder chamber, thereby can simplified structure and save raw and auxiliary material.
The accompanying drawing explanation
Fig. 1 is the embodiments of the invention structure chart.
The detailed structure view that Fig. 2 is the signal pickup assembly shown in Fig. 1.
The specific embodiment
For the auditor that the makes Patent Office especially public can be expressly understood technical spirit of the present invention and beneficial effect more, the applicant general elaborates in the mode of embodiment below, but the description to embodiment is not all the restriction to the present invention program, any according to the present invention design, done only for pro forma but not substantial equivalent transformation all should be considered as technical scheme category of the present invention.
Every concept that relates to the directionality of upper and lower, left and right (comprising the upper end of short transverse, lower end and the short transverse middle part of short transverse) and so on or claim directionality, all for by illustrated location status, therefore can not be understood as the specific limited to the present invention program in the following description.
Refer to Fig. 1, provided a cylindrical shell 1, the top of this cylindrical shell 1 forms upper cover 11, and the bottom of cylindrical shell 1 formation has a low head 12, in cylindrical shell 1 and the nearly middle part that is positioned at the short transverse of cylindrical shell 1 be provided with a chamber demarcation strip 2 with level, by this chamber demarcation strip 2, the cylinder chamber of cylindrical shell 1 is divided into to cylindrical shell epicoele 13 and cylindrical shell cavity of resorption 14, the space that upper cover 11 and cylinder chamber demarcation strip 2 form between a upper side specifically is cylindrical shell epicoele 13, and low head 12 and cylinder chamber demarcation strip 2 towards under a side between the space that forms be cylindrical shell cavity of resorption 14, on cylindrical shell, cavity of resorption 13, between 14, by the cavity of resorption filter core liquid outlet mating holes 21 be opened in the interval state on a chamber demarcation strip 2, connect.
As shown in Figure 1, on aforesaid upper cover 11, form a cylindrical shell epicoele man-hole opening 111 is arranged, and sealing is equipped with a manhole lid 1111 on this cylindrical shell epicoele man-hole opening 111.Again, be equipped with a greasy dirt communicated with cylindrical shell epicoele 13 and draw interface 112 on upper cover 11, and draw on interface 112 and be connected with a greasy dirt fairlead 1121 at this greasy dirt, preferred scheme can arrange a greasy dirt fairlead and open and close valve 11211 on the pipeline of this greasy dirt fairlead 1121.On low head 12 and the bottom that is positioned at low head 12 be fixed with one group of cylinder bearing pin 121, by this group cylinder bearing pin 121, make cylindrical shell 1 be arranged on the terrace of field of employment with airborne or similarly on carrier.Formation has a cylindrical shell cavity of resorption inspection mouth 15 (also can to claim position) on the sidewall of cylindrical shell 1 and in the zone corresponding to cylindrical shell cavity of resorption 14, and on this cylindrical shell cavity of resorption inspection mouth 15, sealing is equipped with a cylindrical shell cavity of resorption inspection lid 151.Preferred scheme also can be designed to transparence (using transparent implosion guard) by this cylindrical shell cavity of resorption inspection lid 151.
Provided one group of cavity of resorption filter core 3, the quantity of this group of cavity of resorption filter core 3 equates with the quantity of aforementioned cavity of resorption filter core liquid outlet mating holes 21, and each cavity of resorption filter core 3 preferably is positioned at cylindrical shell cavity of resorption 14 with the vertical cantilever state, the cavity of resorption filter core liquid outlet 31 of each cavity of resorption filter core 3 matches with cavity of resorption filter core liquid outlet mating holes 21, is fixed on cavity of resorption filter core liquid outlet mating holes 21.
As shown in the above description, each cavity of resorption filter core liquid outlet mating holes 21 is assigned a cavity of resorption filter core 3, and 3 employings of cavity of resorption filter core by Chinese utility model patent ZL200920255310.2(notification number are: structure CN201529434U).In addition because the reading by ZL200920255310.2 is appreciated that coordinating of cavity of resorption filter core 3 and cavity of resorption filter core liquid outlet mating holes 21 fully, so the applicant repeats no more.
Having provided one introduces the aforementioned cavity of resorption filter core 3 of the interior confession of aforementioned cylindrical shell cavity of resorption 14 to implement that essence filters is a condensate water inlet tube 4 of precision processing for the condensate water that essence filters of awaiting after being processed by preceding working procedure, one end of this condensate water inlet tube 4 and the bottom of low head 12 are fixed, and communicate with cylindrical shell cavity of resorption 14, and the other end is configured to inlet tube water inlet 42, this inlet tube water inlet 42 by pipeline and preceding working procedure for example the active carbon filter delivery port of active carbon filter be connected.
A spacer cylinder 5 and a return pipe 6 have been provided, spacer cylinder 5 be fixed on aforementioned upper cover 11 towards a side of cylindrical shell epicoele 13 be fixed on upper cover 11 towards under a side and corresponding to the middle position (middle position) of upper cover 11, a side at spacer cylinder 5 is extended with a spacer cylinder water inlet interface 52, this spacer cylinder water inlet interface 52 communicates with the spacer cylinder chamber 51 of spacer cylinder 5, and is equipped with a check valve 521 on this spacer cylinder water inlet interface 52.In to the condensate fine processing procedure, the cavity of resorption filter core liquid outlet 31 from cavity of resorption filter core 3 after cavity of resorption filter core 3 filters of the water in cylindrical shell cavity of resorption 14 is introduced in cylindrical shell epicoele 13, and enters into the interior water of cylindrical shell epicoele 13 in check valve 521 enters spacer cylinder chamber 51.One end of return pipe 6 is stretched in cylindrical shell epicoele 13 and with spacer cylinder 5 and is connected through upper cover 11 from upper cover 11.Because return pipe 6 communicates with spacer cylinder chamber 51, the water therefore entered in spacer cylinder chamber 51 is drawn by return pipe 6, as the make-up water use of boiler.As shown in Figure 1, the other end of return pipe 6 is positioned at outside cylinder chamber and is vertical parallel state with cylindrical shell 1 and stretches downwards, be respectively arranged with compressed air in the end of the other end of this return pipe 6 and introduce interface 61, from flushing water water inlet interface 62, water outlet mouthpiece 63 and backwashing water, introduce interface 64, the function of these interfaces also will be mentioned below.
Preferably, the lower end of aforesaid return pipe 6 is fixed by return pipe holder 65 and the outer wall of cylindrical shell 1.
Please continue to see Fig. 1, show a backwash tube driving mechanism 7 and a backwash tube 8, backwash tube driving mechanism 7 is arranged on aforementioned upper cover 11 back to a side of cylindrical shell epicoele 13 and corresponding with spacer cylinder 5, the upper end of backwash tube 8 is stretched in the spacer cylinder chamber 51 of spacer cylinder 5, and with backwash tube driving mechanism 7, be in transmission connection, and the lower end of backwash tube 8 is bearing in the middle position of aforementioned cylinder chamber demarcation strip 2 rotationally by backwash tube axle bed 84.Sidepiece in the lower end of backwash tube 8 forms to have and offers a backwash tube liquid outlet 81.
Technical essential as technical scheme provided by the invention, in the lower end of aforesaid backwash tube 8 and be fixed with a counter-flushing liquid spray arm 82 in the position corresponding to backwash tube liquid outlet 81 with the horizontal boom state, this counter-flushing liquid spray arm 82 is corresponding to the top of cylinder chamber demarcation strip 2, and form a spray arm opening 821 is arranged in the bottom of the length direction of this counter-flushing liquid spray arm 82, this spray arm opening 821 communicates with the counter-flushing liquid spray arm chamber 822 of counter-flushing liquid spray arm 82, and counter-flushing liquid spray arm chamber 822 communicates with backwash tube liquid outlet 81.Hence one can see that, when backwash, the counter-flushing liquid of being introduced by backwash tube 8 is the counter-flushing liquid spray arm chamber 822 that backwashing water self counter flushing pipe liquid outlet 81 is introduced counter-flushing liquid spray arm 82, and then in the cavity of resorption filter core liquid outlet 31(backwash process of the aforesaid cavity of resorption filter core 3 of spray arm opening 821 directive, this cavity of resorption filter core liquid outlet 31 develops into cavity of resorption filter core inlet), the cavity of resorption filter core is implemented to backwash.
As shown in Figure 1, a side of the length direction of counter-flushing liquid spray arm 82 and opposite side and be positioned at counter-flushing liquid spray arm 82 bottom each form a liquid outlet sealing block wing 823 that leans out the lateral surface (lateral surface of bottom) of counter-flushing liquid spray arm 82 arranged, because liquid outlet sealing block wing 823 pastes and touch (being aforesaid the contact) towards a side of cylindrical shell epicoele 13 towards a upper side with cylinder chamber demarcation strip 2, thereby the cavity of resorption filter core liquid outlet 31 that can seal the both sides of 823 pairs of non-length directions that are positioned at counter-flushing liquid spray arm 82 under spray arm opening 821 of block wing by liquid outlet covers, guarantee that the counter-flushing liquid in counter-flushing liquid spray arm chamber 822 is able to by spray arm opening 821 to the effective backwash of cavity of resorption filter core liquid outlet 31 that is right against the one below.More particularly, make spray arm opening 821 under desirable water flow pressure, spray to cavity of resorption filter core liquid outlet 31 with the state that The turbulent river crashes its way through, embody the ultimate attainment backwash effect to cavity of resorption filter core 3.
As shown in Figure 1, be equipped with the logical liquid joint 83 of a backwash tube in the upper end of aforesaid backwash tube 8, the upper end of the logical liquid joint 83 of this backwash tube is positioned at the spacer cylinder chamber 51 of aforementioned spacer cylinder 5, with aforesaid backwash tube driving mechanism 7, be fixedly connected with, and offer fluid-through tube joint liquid-through hole 831 with the interval state on the wall body of the upper end of the logical liquid joint 83 of backwash tube, by fluid-through tube joint liquid-through hole 831, the fluid-through tube joint chamber of the logical liquid joint 83 of backwash tube is communicated with spacer cylinder chamber 51, the lower end of the logical liquid joint 83 of backwash tube is stretched over outside spacer cylinder chamber 51 and by logical liquid joint flange 832 and is fixedly connected with the backwash tube flange 85 that the upper end port position of backwash tube 8 forms.
As preferred scheme, the diameter of aforesaid counter-flushing liquid spray arm 82 diminishes towards the direction away from backwash tube liquid outlet 81 gradually from described backwash tube liquid outlet 81, and the length of counter-flushing liquid spray arm 82 adapts with the radius of aforesaid cylinder chamber demarcation strip 2 substantially, here, why the applicant claims " substantially ", be because considered the radius of backwash tube 8, that is to say that the length of counter-flushing liquid spray arm 82 adds backwash tube 8(backwash tube 8 for pipe) radius equal a radius of chamber demarcation strip 2.
Please see Fig. 1 and Fig. 2 by emphasis, above mentioned backwash tube driving mechanism 7 is preferably but not definitely to be limited to ground structure as follows: comprise backwash motor 71, backwash reductor 72, shaft coupling 73, backwash reductor supporting base 74, main shaft 75, signal panels 76 and signal pickup assembly 77, backwash motor 71 is in transmission connection with backwash reductor 72, and be fixed on the top of backwash reductor supporting base 74 together with backwash motor 71 by backwash reductor 72, and the bottom of backwash reductor supporting base 74 is fixed back to the middle position of a side of cylindrical shell epicoele 13 by one group of supporting base hold-down screw 741 and aforesaid upper cover 11, and corresponding with aforesaid spacer cylinder 5.Shaft coupling 73 is connected between the upper end of the backwash speed reducer output shaft 721 of backwash reductor 72 and main shaft 75, hence one can see that, the function of shaft coupling 73 is that backwash speed reducer output shaft 721 is connected with the upper end of main shaft 75, the lower end of main shaft 75 is stretched in the spacer cylinder chamber 51 of spacer cylinder 5, and with the top of the logical liquid joint 83 of the aforementioned backwash tube of backwash tube 8 be in transmission connection (being fixedly connected with).Signal panels 76 are nested with on main shaft 75, and fixing with shaft coupling 73, on these signal panels 76 and around the edge of the circumferencial direction of signal panels 76, with the equidistant intervals state, offer one group of telltale hole 761.Signal pickup assembly 77 is fixed on backwash reductor supporting base 74, and be positioned at signal panels 76 below corresponding with telltale hole 761, this signal pickup assembly 77 and aforesaid backwash motor 71 are connected with the electric control box electrical control by circuit.
Preferably, aforesaid shaft coupling 73 comprises shaft coupling 731, lower shaft coupling 732 and one group of shaft coupling attachment screw 733, upper shaft coupling 731 adopts flat key and backwash speed reducer output shaft 721 keys to be connected and fixed, and should towards an end formation of lower shaft coupling 732, shaft coupling terminal pad 7311 on be arranged by upper shaft coupling 731, the same top key of flat key and main shaft 75 that preferably adopts of lower shaft coupling 732 is connected and fixed, and this time shaft coupling 732 has shaft coupling terminal pad 7321 towards an end formation of upper shaft coupling 731, on, lower shaft coupling terminal pad 7311, 7321 be fitted to each other and by shaft coupling screw 733 by upper, lower shaft coupling terminal pad 7311, 7321 are fixed together.Aforesaid signal panels 76 are fixing with lower shaft coupling 732.
Aforesaid signal pickup assembly 77 comprises signal picker support 771 and signal picker 772, signal picker support 771 use pair of brackets hold-down screws 7711 are fixed on backwash reductor supporting base 74, signal picker 772 is fixed on signal picker support 771, and be positioned at signal panels 76 below corresponding with aforementioned telltale hole 761, signal picker 772 is connected with above mentioned electric control box electrical control by signal picker circuit 7721.
Offer one group of adjustment tank 762 with the interval state on aforesaid signal panels 76 and in the position corresponding to lower shaft coupling 732, respectively be equipped with an adjustment tank attachment screw 7621 in the position corresponding to each adjustment tank 762, each adjustment tank attachment screw 7621 is fixed towards an end end face of signal panels 76 with lower shaft coupling 762, that is, with lower shaft coupling 732 towards under the end face of an end be fixedly connected with.
Preferably, because signal panels 76 are disc, so adjustment tank 762 is arc-shaped slot (also can claim deep-slotted chip breaker).
Preferably, aforesaid signal picker 772 is photoelectric sensor.
The applicant it should be noted that: if by aforesaid one group of telltale hole 761 change into one group be raised in signal panels 76 towards under the signal flange on surface of a side, and use aforesaid signal picker 772 instead travel switch or microswitch, should be considered as so and technology contents equivalent disclosed by the invention; And for example fruit is used aforesaid one group of telltale hole 761 instead one group of magnet steel, and uses signal picker 772 instead tongue tube or hall sensing element, so still is considered as and technology contents equivalent disclosed by the invention.Therefore, any change telltale hole 761 and signal picker 772(photoelectric sensor) fit form all should be considered as protection scope of the present invention.
When normal operation, be in the process of the present invention in the condensate water processing to awaiting precision processing, close the valve on the pipeline of blowdown interface 41 of condensate water inlet tube 4, open the valve on the pipeline matched with inlet tube water inlet 42, the condensate water that awaits precision processing just enters in cylindrical shell cavity of resorption 14 from condensate water inlet tube 4, for the one group of cavity of resorption filter core 3 in cylindrical shell cavity of resorption 14, filters.Water after filtration enters in cylindrical shell epicoele 13 from cavity of resorption filter core liquid outlet 31, the water entered in cylindrical shell epicoele 13 enters in spacer cylinder chamber 51 through check valve 521 and spacer cylinder water inlet interface 52 successively, because an end of return pipe 6 communicates with spacer cylinder chamber 51, therefore by the water outlet mouthpiece 63 of return pipe 6, drawn and the water used as boiler feedwater.In this process, compressed air is introduced interface 61, positive flushing water water inlet interface 62 and backwashing water and is introduced interface 64 all in closed condition.
When condensate fine processor of the present invention after operation a period of time, when the pressure reduction between condensate water inlet tube 4 and return pipe 6 reaches settings and for example reaches 0.15MPa, so by pressure difference transmitter by signal feedback to electric control box, enter backwashing procedures.Preferred scheme can arrange Pressure gauge (specifically can referring to patent of invention publication No. CN103301682A) on the pipeline of return pipe 6.
Backwashing procedures has two kinds of control modes, the one, automatic control, adopt programmable controller (PLC) to control, during backwash according to the signal of pressure difference transmitter by PLC switching controls valve and order about backwash motor 71 work of backwash tube driving mechanism 7, drive backwash reductor 72 by backwash motor 71 under this state, drive main shaft 75 rotations by backwash speed reducer output shaft 721 through shaft coupling 73 under the state slowed down at backwash reductor 72, because the signal panels 76 that are nested with on main shaft 75 are fixedly connected with the lower shaft coupling 732 of shaft coupling 73 by the adjustment tank attachment screw 7621 on adjustment tank 762, therefore when driving main shaft 75 rotations, shaft coupling 73 drives signal panels 76 rotations, telltale hole 761 on signal panels 76 is during corresponding to signal picker 772, by signal picker 772 by signal feedback to PLC, sending signal by PLC temporarily quits work backwash motor 71, dwell time is arranged by PLC, be generally several seconds kinds 5-10 seconds for example.In this process, introduce interface 64 by backwashing water backwashing water is introduced to return pipe 6, due to check valve 521 now in closed condition, therefore the water entered in return pipe 6 enters in the spacer cylinder chamber 51 of spacer cylinder 5, the upper end that leads to liquid joint 83 due to backwash tube is positioned at spacer cylinder chamber 51, and because the fluid-through tube joint liquid-through hole 831 on the wall body of the logical liquid joint 83 of backwash tube communicates with spacer cylinder chamber 51, so the fluid-through tube joint liquid-through hole 831 of the water in spacer cylinder chamber 51 on the logical liquid joint 83 of backwash tube introduced in logical liquid joint.Again because logical liquid joint communicates with the backwash tube chamber of backwash tube 8, also because counter-flushing liquid spray arm 82 communicates with the backwash tube liquid outlet 81 of backwash tube 8 lower ends, therefore introduce the backwashing water of interface 64 introducings successively through return pipe 6 through backwashing water, spacer cylinder chamber 51, fluid-through tube joint liquid-through hole 831, the backwash tube liquid outlet 81 of backwash tube 8 enters the counter-flushing liquid spray arm chamber 822 of counter-flushing liquid spray arm 82, until be injected into cavity of resorption filter core liquid outlet 31 by the spray arm opening 821 communicated with counter-flushing liquid spray arm chamber 822, cavity of resorption filter core 3 that be connected with cavity of resorption filter core liquid outlet mating holes 21 and that be positioned at cylindrical shell cavity of resorption 14 is implemented to backwashes.When the time of setting, arrive, PLC sends instruction so, make backwash motor 71 task again, until make next signal hole 761 on signal panels 76 corresponding to signal picker 772, so repeat and until make counter-flushing liquid spray arm 82 backwash tube 8 with 360 ° of state revolutions at intermittence process in all cavity of resorption filter cores 3 are implemented to backwashes.After backwash finishes, more just rinsing, then turning back to the aforesaid state that former water processed the condensate water that awaits precision processing.The 2nd, manual control, on cylindrical shell 1 or follow in cylindrical shell 1 place electric control box is set, switch valve when pressure reduction reaches setting value, and start 71 work of backwash motor, by the superincumbent description of applicant, until counter-flushing liquid spray arm 82 completes the backwash to the cavity of resorption filter core 3 in cylindrical shell cavity of resorption 14 around cylinder chamber demarcation strip 2 one circles (360 °).
After with automated manner or with manual mode, having completed backwash, enter positive rinsing step, just rinsing is mainly the impurity of bringing in backwashing water and gas while rinsing out backwash.While just rinsing, valve opening on the pipeline be connected with the inlet tube water inlet 42 of condensate water inlet tube 4, and the valve closing on blowdown interface 41, water outlet mouthpiece 63 on the pipeline of return pipe 6, compressed air introduce interface 61 and backwashing water is introduced interface 64 all in closed condition, and positive flushing water water inlet interface 62 rinses rear condensate fine processor of the present invention and enters again the state of coming into operation in opening.
In cavity of resorption filter core 3 is carried out to the process of backwash, the valve closing on the passage of the inlet tube water inlet 42 of condensate water inlet tube 4,41 unlatchings of blowdown interface; Valve opening on the passage that the backwashing water introducing interface 64 of return pipe 6 and compressed air are introduced interface 61 (be take and enabled compressed air as example simultaneously, if do not enable, the closes compression air is introduced the valve on the pipeline of interface 61 so), the valve closing on the passage of water outlet mouthpiece 63, positive flushing water water inlet interface 62.
By the explanation above-mentioned to the applicant, can know that the backwash effect to cavity of resorption filter core 3 that the present invention shows should be ultimate attainment fully.
In sum, technical scheme provided by the invention has overcome the shortcoming in the prior art, has completed the invention task, has cashed the technique effect referred in the superincumbent technique effect of applicant hurdle.

Claims (10)

1. a kind of condensate fine processor, comprise that top forms and upper cover (11) to be arranged and bottom forms the cylindrical shell (1) that low head (12) is arranged, a chamber demarcation strip (2), this chamber demarcation strip (2) is arranged in the cylinder chamber of cylindrical shell (1) and by this chamber demarcation strip (2), the cylinder chamber of cylindrical shell (1) is divided into to cylindrical shell epicoele (13) and cylindrical shell cavity of resorption (14) with level, at this chamber demarcation strip (2), goes up and offers one group of cavity of resorption filter core liquid outlet mating holes (21) with the interval state, one group of cavity of resorption filter core (3), the quantity of this one group of cavity of resorption filter core (3) equates with the quantity of described cavity of resorption filter core liquid outlet mating holes (21), and in the position corresponding to cavity of resorption filter core liquid outlet mating holes (21), with vertical state, be arranged in described cylindrical shell cavity of resorption (14), the cavity of resorption filter core liquid outlet (31) of each cavity of resorption filter core (3) matches with cavity of resorption filter core liquid outlet mating holes (21), one introduces for the condensate water that will await the essence filtration condensate water inlet tube (4) filtered for described cavity of resorption filter core (3) in described cylindrical shell cavity of resorption (14), this condensate water inlet tube (4) is fixed with the bottom of described low head (12), and communicates with cylindrical shell cavity of resorption (14), one spacer cylinder (5) and a return pipe (6), spacer cylinder (5) is fixed on described upper cover (11) towards a side of described cylindrical shell epicoele (13) and corresponding to the middle position of upper cover (11), a side of spacer cylinder (5) be extended with one with the spacer cylinder chamber (51) of spacer cylinder (5), communicate introduce a spacer cylinder in spacer cylinder chamber (51) interface (52) of intaking for the water by cylindrical shell epicoele (13), be provided with a check valve (521) on this spacer cylinder water inlet interface (52), one end of return pipe (6) is in described upper cover (11) is stretched over described cylindrical shell epicoele (13), be connected with described spacer cylinder (5) and communicate with described spacer cylinder chamber (51), the other end of return pipe (6) is stretched over outside cylinder chamber, one backwash tube driving mechanism (7) and a backwash tube (8), backwash tube driving mechanism (7) is arranged on described upper cover (11), and corresponding with described spacer cylinder (5), the upper end of backwash tube (8) is stretched in described spacer cylinder chamber (51), and be in transmission connection with backwash tube driving mechanism (7), and the lower end of backwash tube (8) is bearing in the middle position of described cylinder chamber demarcation strip (2) rotationally, and the sidepiece in the lower end of this backwash tube (8) offers a backwash tube liquid outlet (81), it is characterized in that: in the lower end of described backwash tube (8) and be fixed with a counter-flushing liquid spray arm (82) in the position corresponding to described backwash tube liquid outlet (81) with the horizontal boom state, this counter-flushing liquid spray arm (82) is corresponding to the top of described cylinder chamber demarcation strip (2), and form a spray arm opening (821) is arranged in the bottom of the length direction of this counter-flushing liquid spray arm (82), this spray arm opening (821) communicates with the counter-flushing liquid spray arm chamber (822) of counter-flushing liquid spray arm (82), and counter-flushing liquid spray arm chamber (822) communicates with backwash tube liquid outlet (81).
2. condensate fine processor according to claim 1, it is characterized in that forming cylindrical shell cavity of resorption inspection mouth (15) being arranged on the sidewall of described cylindrical shell (1) and in the position corresponding to described cylindrical shell cavity of resorption (13), in the upper sealing of this cylindrical shell cavity of resorption inspection mouth (15), be equipped with a cylindrical shell cavity of resorption inspection lid (151); In the upper formation of described upper cover (11), one cylindrical shell epicoele man-hole opening (111) is arranged, be equipped with a manhole lid (1111) in the upper sealing of this cylindrical shell epicoele man-hole opening (111), and be equipped with a greasy dirt and draw interface (112) on upper cover (11), this greasy dirt is drawn interface (112) and is communicated with cylindrical shell epicoele (13), and draws on interface (112) and be connected with a greasy dirt fairlead (1121) at this greasy dirt; Be fixed with one group of cylinder bearing pin (121) on described low head (12).
3. condensate fine processor according to claim 1, is characterized in that being equipped with a blowdown interface (41) on the pipeline of described condensate water inlet tube (4).
4. condensate fine processor according to claim 1, is characterized in that being equipped with a compressed air introducing interface (61), a positive flushing water water inlet interface (62), a water outlet mouthpiece (63) and backwashing water introducing interface (64) at the described other end of described return pipe (6).
5. condensate fine processor according to claim 1, it is characterized in that described backwash tube driving mechanism (7) comprises backwash motor (71), backwash reductor (72), shaft coupling (73), backwash reductor supporting base (74), main shaft (75), signal panels (76) and signal pickup assembly (77), backwash motor (71) is in transmission connection with backwash reductor (72), and be fixed on backwash reductor supporting base (74) together with backwash motor (71) by backwash reductor (72), and backwash reductor supporting base (74) is fixed on described upper cover (11), and be positioned at the middle position of upper cover (11), shaft coupling (73) is connected between the backwash speed reducer output shaft (721) and main shaft (75) of backwash reductor (72), main shaft (75) is stretched in the spacer cylinder chamber (51) of described spacer cylinder (5) and is in transmission connection with described backwash tube (8), signal panels (76) are nested with on main shaft (75), and fixing with shaft coupling (73), upper and offer one group of telltale hole (761) around the circumferencial direction of signal panels (76) with the equidistant intervals state at these signal panels (76), signal pickup assembly (77) is fixed on backwash reductor supporting base (74), and corresponding with described telltale hole (761), this signal pickup assembly (77) is connected with the electric control box electrical control by circuit, and described backwash motor (71) is connected with the electric control box electrical control equally.
6. condensate fine processor according to claim 5, it is characterized in that described shaft coupling (73) comprises, lower shaft coupling (731, 732) and one group of shaft coupling attachment screw (733), upper shaft coupling (731) is connected and fixed with described backwash speed reducer output shaft (721) key, and should towards an end formation of lower shaft coupling (732), shaft coupling terminal pad (7311) on be arranged by upper shaft coupling (731), lower shaft coupling (732) is connected and fixed with described main shaft (75) key, and this time shaft coupling (732) has shaft coupling terminal pad (7321) towards an end formation of upper shaft coupling (731), on, lower shaft coupling terminal pad (7311, 7321) be fitted to each other, one group of shaft coupling attachment screw (733) is with the interval distributions and by upper, lower shaft coupling terminal pad (7311, 7321) be fixed together, described signal panels (76) are fixing with described lower shaft coupling (732), be equipped with the logical liquid joint (83) of a backwash tube in the upper end of described backwash tube (8), the upper end of the logical liquid joint (83) of this backwash tube is positioned at described spacer cylinder chamber (51), with described main shaft (75), be fixedly connected with, and offer fluid-through tube joint liquid-through hole (831) with the interval state on the wall body of the upper end of the logical liquid joint (83) of this backwash tube, fluid-through tube joint liquid-through hole (831) communicates with spacer cylinder chamber (51), the lower end of the logical liquid joint (83) of backwash tube is stretched over outside spacer cylinder chamber (51) and is fixedly connected with backwash tube (8).
7. condensate fine processor according to claim 5, it is characterized in that described signal pickup assembly (77) comprises signal picker support (771) and signal picker (772), signal picker support (771) is fixed on described backwash reductor supporting base (74), signal picker (772) is fixed on signal picker support (771), and corresponding with described telltale hole (761) in the below that is positioned at described signal panels (76), this signal picker (772) is connected with described electric control box electrical control by signal picker circuit (7721).
8. condensate fine processor according to claim 6, it is characterized in that upper at described signal panels (76) and offer one group of adjustment tank (762) in the position corresponding to described lower shaft coupling (732) with the interval state, respectively be equipped with an adjustment tank attachment screw (7621) in the position corresponding to each adjustment tank (762), each adjustment tank attachment screw (7621) is fixed towards an end end face of signal panels (76) with described lower shaft coupling (732), and described adjustment tank (762) is arc-shaped slot.
9. condensate fine processor according to claim 7, is characterized in that described signal picker (772) is photoelectric sensor.
10. condensate fine processor according to claim 1, the diameter that it is characterized in that described counter-flushing liquid spray arm (82) diminishes towards the direction away from backwash tube liquid outlet (81) gradually from described backwash tube liquid outlet (81), and the radius of the length of counter-flushing liquid spray arm (82) and described cylinder chamber demarcation strip (2) adapts, wherein: a side of the length direction of counter-flushing liquid spray arm (82) and opposite side and be positioned at counter-flushing liquid spray arm (82) bottom each form a liquid outlet sealing block wing (823) for described cavity of resorption filter core liquid outlet (31) is covered that leans out the lateral surface of counter-flushing liquid spray arm (82) arranged, liquid outlet sealing block wing (823) contacts with described cylinder chamber demarcation strip (2).
CN201310448040.8A 2013-09-27 2013-09-27 Precision treater for condensed water Active CN103480193B (en)

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CN110681201A (en) * 2019-11-01 2020-01-14 殷富新 Efficient filtration treatment system for domestic sewage and sewage treatment method thereof
CN115385427A (en) * 2022-09-22 2022-11-25 永城开控水务有限公司 Coal chemical industry gasification waste water treatment equipment

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CN103301682A (en) * 2013-06-05 2013-09-18 常熟市华能水处理设备有限责任公司 Surface condensation liquid filter
CN203469605U (en) * 2013-09-27 2014-03-12 常熟市华能水处理设备有限责任公司 Fine processor for condensed water

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WO2010097233A2 (en) * 2009-02-27 2010-09-02 Gneuss Kunststofftechnik Gmbh Liquid ring vacuum pump for degassing plastic melts
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CN110681201A (en) * 2019-11-01 2020-01-14 殷富新 Efficient filtration treatment system for domestic sewage and sewage treatment method thereof
CN115385427A (en) * 2022-09-22 2022-11-25 永城开控水务有限公司 Coal chemical industry gasification waste water treatment equipment
CN115385427B (en) * 2022-09-22 2024-03-08 永城开控水务有限公司 Coal chemical industry gasification waste water treatment equipment

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