CN2723428Y - Large plate type evaporator - Google Patents
Large plate type evaporator Download PDFInfo
- Publication number
- CN2723428Y CN2723428Y CN 200420085992 CN200420085992U CN2723428Y CN 2723428 Y CN2723428 Y CN 2723428Y CN 200420085992 CN200420085992 CN 200420085992 CN 200420085992 U CN200420085992 U CN 200420085992U CN 2723428 Y CN2723428 Y CN 2723428Y
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- plate
- pipe
- steam
- well heater
- type evaporator
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Abstract
The utility model relates to the large-scale equipment used for evaporating and concentrating liquid. The utility model comprises a bracket, a casing arranged on the bracket, a heating element which is arranged inside the casing, composed of the evaporation plate bundles, and is fixed by adopting a suspended structure inside the casing, a heating steam inlet pipe and a condensing water discharge pipe which are arranged on the heating element, a recovered steam outlet pipe and a condensing liquid outlet which are arranged on the casing, an evaporated liquid inlet pipe, a liquid membrane distributor which is arranged at the evaporated liquid inlet pipe and the top of the heater plate, and a mist eliminator which is arranged on the upper course of the recovered steam discharge pipe. The utility model adopts the evaporation heating plate whose width is 1. 22-1. 5 meters, the length is 7. 5-12. 0 meters, and the width of the inner part of the plate cavity is 15-20 mm.
Description
Technical field
The utility model relates to and a kind of liquid is carried out the main equipment of evaporation concentration, particularly is applicable to the evaporation concentration equipment that paper industry is handled waste water, and the steam output of its single device can reach 100t/h.Comprise support in the utility model, be located at the shell on the support, be located at the fixed of the employing suspended structure in the enclosure heating unit that constitutes by evaporation plate bundle of enclosure, be located at heating steam inlet pipe and condensed water discharge pipe on the heating unit, be located at secondary steam outlet pipe and condensate outlet on the shell, be evaporated liquid inlet tube, be located at the liquid film divider that is evaporated liquid inlet tube and well heater plate top, and the scum dredger of being located at secondary steam vent pipe upstream.
Background technology
Along with developing rapidly of China's papermaking enterprise, paper output is increasing, the papermaking wastewater amount also increases thereupon, if the evaporator station of liquid waste treatment system adopts the plate-type evaporator (annotate: the maximum textryl of vaporizer is of a size of 1.22 * 7.32 in the prior art) of existing structure size, then must make the diameter of the housing of single device very big, and a plurality of plate bundles assemble in housing and also make its technology and inner pipeline more complicated, and it is reasonable, economical that its device structure design is difficult to accomplish.In addition, the multiple-effect evaporation station floor space of being made up of many platens formula vaporizer is also bigger.The multiple row evaporator station mode that adopts is also arranged in the prior art, though this mode can make the scantlings of the structure of single device reduce, whole evaporator station floor space can be bigger, and total system pipeline and control is more complicated, and investment accordingly also can be very big.Therefore, for adapting to the development of papermaking enterprise, it is very urgent to develop out a kind of large-scale plate-type evaporator.
Summary of the invention
The utility model provides a kind of insufficient large-scale plate-type evaporator of prior art that overcomes.
The vaporizer heating plates width that the utility model adopted is 1.22～1.5 meters, and length is 7.5～12.0 meters, and the width of its inside, plate chamber is 15～20 millimeters.
Because the utility model has adopted bigger heater plates chip architecture, though can solve the difficulty of major diameter evaporator designs, manufacturing process in the prior art, and the equipment installation complexity, the deficiency that floor space is big, but big textryl also can bring some shortcomings.As: strengthen with the plate cavity space, the incondensable gas quantity that together enters the plate inner chamber with steam also can increase, and can assemble in the plate chamber, causes heat exchange efficiency to reduce; Because becoming its thermal distortion of ambassador, strengthens in device; Because the plate lengthening, what plate bottom possibility thermo-efficiency became when device work is lower, etc.For solve these because of plate strengthens issuable problem, the utility model is taked following technical measures:
On heating unit, be provided with the non-condensable gas vent pipe, so that non-condensable gas is discharged.
Condensation-water drain take over and the non-condensable gas outlet connection on establish expansion joint respectively, with overcome device be heated the back generation deformation and cause the impaired destruction of device.
At least being provided with one group in the enclosure is used for to hanging the support that the fixed well heater carries out lateral confinement, with the side throw that its lower end produces when hanging fixedly of constraint length plate.
For solving well heater plate lengthening, cause the lower deficiency of plate lower end temperature, the utility model heating steam inlet pipe is provided with the additional steam inlet pipe of part steam being introduced the well heater lower end, and the position that replenishes steam inlet pipe access well heater is positioned at 2/3rds to 1/2nd places of well heater plate height.
On shell, be provided with simultaneously expansion joint, the problems that cause with the thermal distortion that overcomes crust of the device.
The additional steam that the utility model can also be provided with in the lower end of well heater part steam introducing well heater lower end enters pipe, the interface that set additional steam enters between pipe and well heater is positioned at 2/3rds to 1/2nd places of well heater plate height, in the inside in well heater plate plate chamber and replenishing steam and enter on the interface between pipe and well heater and be provided with the top water of condensation not exclusively every road and epimere condensed water discharge pipe, and epimere non-condensable gas relief outlet.The water of condensation that this structure can make top, heater plates chamber produce comes together in not exclusively in the road, and from epimere condensed water discharge pipe discharge system, and the non-condensable gas that is collected in well heater plate top is discharged system by epimere non-condensable gas relief outlet, heating steam simultaneously can enter the lower end of managing reheater plate inner chamber by replenishing steam, and the whole vaporization efficiency of device is improved.
For overcoming the thermal distortion of device, the utility model is that shell is provided with expansion joint, and described expansion joint should be arranged at the heating steam pipe and lower end steam enters between the pipe.
The utlity model has following advantage:
1, because the utility model has adopted bigger plate size, can make the housing external diameter of single device be unlikely to very big, and the plate bundle comparatively oversimplifies in housing gut line assembling, and its device structure design can be more reasonable, economical, can also reduce the area that evaporator station takes up an area of;
2, because heating unit is provided with the non-condensable gas vent pipe, the noncondensable gas of bringing into steam is overflowed, avoid the gathering of noncondensable gas in heating unit, the heat exchange efficiency of device is increased.Particularly the utility model is provided with upper end non-condensable gas vent pipe and the non-condensable gas vent pipe that is positioned at the well heater bottom, and the intravital non-condensable gas of bigger heating chamber is in time discharged;
3, adopt in the enclosure the fixedly structure of heating unit of suspended structure, simultaneously on condensation-water drain adapter and non-condensable gas outlet connection, and expansion joint is set respectively on the shell, and overcome many drawbacks that equipment causes because of cold and hot distortion, alleviate the thermal stresses that thermal expansion causes;
4, the utility model adopts additional steam to enter pipe and provides heating steam to the bottom of heating plates, can overcome the deficiency of long its underpart, plate chamber temperature step-down;
5, particularly the utility model employing is provided with not exclusively every road, epimere non-condensable gas vent pipe and epimere condensed water discharge pipe, and additional steam enters the structure of pipe, the non-condensation gas on well heater plate top can in time be discharged, the water of condensation of condensation is discharged, simultaneously can introduce heating steam, bottom, heater plates chamber is fully heated, make the vaporization efficiency of system be able to abundant raising, give full play to advantage of the present utility model.
Description of drawings
Among the figure:
1 is condensating water outlet tube, 2 is bearing, 3 is manhole, 4 and 15 is non-condensable gas outlet pipes, 5 is shell, 6 is to hanging the support of fixed well heater 7 plate Shu Jinhang lateral confinement, the 7th, well heater, the 8th, the heating steam inlet pipe, the 9th, the liquid film divider, the 10th, the solution inlet port pipe, the 11st, be positioned at the scum dredger of secondary steam outlet pipe upstream, the 12nd, end socket, the 13rd, the secondary steam outlet pipe, the 14th, the taphole pipe, the 16th, be located at the expansion joint on the solution inlet port pipe, the 17th, be located at the expansion joint on the taphole pipe, the 18th, be located at the expansion joint on the shell, the 19th, replenish steam among first kind of embodiment of the present utility model and enter pipe (referring to accompanying drawing 1, in the drawings for making drawing succinct, the additional steam that is positioned at the right side plate that only drawn enters pipe, and the additional steam that has omitted the left side plate enters pipe), the 20th, replenish steam among second kind of embodiment of the utility model and enter pipe, the 21st, plate chamber upper end condensed water discharge pipe among second kind of embodiment of the utility model, the 22nd, plate chamber epimere non-condensation gas vent pipe among second kind of embodiment of the utility model, 23 be in the plate chamber of second kind of embodiment of the utility model not exclusively every the road, 24 is hemisphere blister convex set on the plate, and 25 is epimere non-condensable gas and condensation-water drain among second embodiment.
Embodiment
The utility model illustrates below in conjunction with embodiment:
By accompanying drawing 1 as seen, first kind of embodiment of the present utility model has in the shell 5 of expansion joint 18 thereon, hangs with support and is fixed with the well heater 7 that is made of plate.The position that joins at heating steam inlet pipe 8 and condensating water outlet tube and well heater 7 is respectively equipped with non-condensable gas outlet pipe 4 and 15.The downstream of liquid inlet tube 10 is provided with liquid film divider 9, and will be evaporated the plate outside that liquid is uniformly distributed in well heater by the liquid film divider.Be provided with scum dredger 11 in the upstream of secondary steam outlet pipe 13.Simultaneously also be respectively equipped with expansion joint 16 and 17 on the liquid inlet tube 10 He on the taphole pipe 14.In addition, also be provided with bearing 2 and manhole 3 on the utility model.Be also shown in from figure, heating steam inlet pipe 8 is provided with the additional steam inlet pipe 19 of part steam being introduced the well heater lower end, and to manage 19 inlets that enter in the plate chamber of well heater 7 are 1/3rd to 1/2nd places that are positioned at the plate total height.In addition, in device, be provided with hanging the support 6 that fixed well heater 7 carries out lateral confinement.
The principle of work of present embodiment is: solution to be evaporated is squeezed into solution inlet port 10 by recycle pump, enter on the heat exchange element surface that liquid film divider 9 back is distributed in well heater 7 equably (being on the plate outside surface), and become membranaceous mobile from top to bottom, steam is entered the inner chamber of well heater 7 by steam inlet 8, carry out heat exchange with the liquid film of its outside surface, solution on its outside surface is constantly evaporated, the secondary steam that produces is discharged by secondary steam outlet 13 through scum dredger 11 backs under the depressurized system suction function, is discharged by taphole pipe 14 when concentrated solution concentration reaches set(ting)value.Become water of condensation after the heating steam heat exchange and discharged by condensation-water drain 1, the non-condensable gas that is mixed with in the steam is discharged by non-condensable gas outlet 4/15.Because plate-type evaporator heat exchange of the present utility model meets the film heat-transfer mechanism, enter pipe 19 owing to be provided with supplementary heating steam simultaneously, bottom, plate chamber fully is heated, so its heat transfer efficiency height, evaporation capacity is bigger.
Second kind of embodiment of the present utility model is referring to accompanying drawing 2, its basic structure is identical with first embodiment, but it is directly to introduce from housing that the additional steam in the present embodiment enters pipe 22, in its plate chamber and in the top that additional steam enters pipe 22, be provided with simultaneously not exclusively every road 23, referring to accompanying drawing 3.Additional steam enters the positions of managing 22 settings should be at 1/3rd to 1/2nd places of plate height.As seen from Figure 3 in the plate chamber set not exclusively every road 23 only sealed plate wide about 4/5ths, still leave about 1/5th passage and the chamber conducting of hypomere plate, not exclusively the outlet 25 every road 23 connects end condensed water discharge pipe 21 and epimere non-condensation gas vent pipe 22.From Fig. 3 and Fig. 4, be also shown in and be provided with hemisphere blister convex 24, when forming the plate chamber, the hemisphere blister convex 24 of two plates is arranged relatively, steam is entered produce disturbance behind the plate chamber and breathe heavily stream, the raising heat exchanger effectiveness at each plate.
The basic functional principle of second embodiment is similar to first embodiment, but owing to be provided with not exclusively every road 23 in this example, water of condensation that forms at the inner epimere in when work plate chamber and non-condensable gas come together in not exclusively every the road, and discharge respectively through epimere non-condensation gas vent pipe 21 and the epimere condensed water discharge pipe 22 be located in the outlet 25.Because the water of condensation of epimere is discharged from, replenish the introducing of steam in addition, can make hypomere plate chamber keep higher heat exchange efficiency.
What need special instruction is also the hemispherical protuberances structure should be set on the plate of first embodiment.
Claims (8)
1, a kind of large-scale plate-type evaporator, comprise: bearing, be located at the shell on the support, be located at the fixed of the employing suspended structure in the enclosure heating unit that constitutes by evaporation plate bundle of enclosure, be located at heating steam inlet pipe and condensed water discharge pipe on the heating unit, be located at secondary steam outlet pipe and condensate outlet on the shell, be evaporated liquid inlet tube, be located at the liquid film divider that is evaporated liquid inlet tube and well heater plate top, and the scum dredger of being located at secondary steam vent pipe upstream, the plate width that it is characterized in that vaporizer is 1.22～1.5 meters, the plate length of vaporizer is 7.5～12.0 meters, and the width of its inside, plate chamber is 15～20 millimeters.
2, large-scale plate-type heat exchanger according to claim 1 is characterized in that heating unit is provided with the non-condensable gas vent pipe.
3, large-scale plate-type evaporator according to claim 2 is characterized in that establishing expansion joint respectively on condensation-water drain adapter and the non-condensable gas outlet connection.
4, large-scale plate-type evaporator according to claim 3 is characterized in that being provided with at least in the shell one group and is used for hanging the support that the fixed well heater carries out lateral confinement.
5, according to the described arbitrary large-scale plate-type evaporator of claim 1 to 4, it is characterized in that the heating steam inlet pipe is provided with the additional steam inlet pipe of part steam being introduced the well heater lower end, the position that replenishes steam inlet pipe access well heater is positioned at 2/3rds to 1/2nd places of well heater plate height.
6, large-scale plate-type evaporator according to claim 5 is characterized in that shell is provided with expansion joint.
7, according to the described arbitrary large-scale plate-type evaporator of claim 1 to 4, it is characterized in that the additional steam that is provided with part steam introducing well heater lower end in the lower end of well heater enters pipe, the interface that additional steam enters between pipe and well heater is positioned at 2/3rds to 1/2nd places of well heater plate height, in the inside in well heater plate plate chamber and replenishing steam and enter on the interface between pipe and well heater and be provided with the top water of condensation not exclusively every road and epimere condensed water discharge pipe, and epimere non-condensable gas relief outlet.
8, large-scale plate-type evaporator according to claim 7 is characterized in that shell is provided with expansion joint, and expansion joint is arranged at the heating steam pipe and lower end steam enters between the pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420085992 CN2723428Y (en) | 2004-09-10 | 2004-09-10 | Large plate type evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420085992 CN2723428Y (en) | 2004-09-10 | 2004-09-10 | Large plate type evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2723428Y true CN2723428Y (en) | 2005-09-07 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200420085992 Expired - Lifetime CN2723428Y (en) | 2004-09-10 | 2004-09-10 | Large plate type evaporator |
Country Status (1)
| Country | Link |
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| CN (1) | CN2723428Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102862038A (en) * | 2012-09-13 | 2013-01-09 | 兰州节能环保工程有限责任公司 | Preparation method of medium- and high-pressure plate heat exchanger and device |
| WO2013120403A1 (en) * | 2012-02-15 | 2013-08-22 | Fu Lijiang | Vacuum rotation film-forming and depressurizing evaporation system |
| CN103466733A (en) * | 2013-09-26 | 2013-12-25 | 沈阳东方钛业股份有限公司 | Water treatment evaporator |
| CN103848464A (en) * | 2014-02-28 | 2014-06-11 | 长沙威保特环保科技有限公司 | Treatment method of low-temperature evaporation high-concentration sewage |
| CN107096248A (en) * | 2017-06-29 | 2017-08-29 | 柳健康 | One kind seven imitates tube sheet combination falling film evaporator technique |
| CN115910410A (en) * | 2023-01-04 | 2023-04-04 | 中国原子能科学研究院 | Method for treating radioactive waste liquid |
-
2004
- 2004-09-10 CN CN 200420085992 patent/CN2723428Y/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013120403A1 (en) * | 2012-02-15 | 2013-08-22 | Fu Lijiang | Vacuum rotation film-forming and depressurizing evaporation system |
| CN102862038A (en) * | 2012-09-13 | 2013-01-09 | 兰州节能环保工程有限责任公司 | Preparation method of medium- and high-pressure plate heat exchanger and device |
| CN103466733A (en) * | 2013-09-26 | 2013-12-25 | 沈阳东方钛业股份有限公司 | Water treatment evaporator |
| CN103466733B (en) * | 2013-09-26 | 2014-10-22 | 沈阳东方钛业股份有限公司 | Water treatment evaporator |
| CN103848464A (en) * | 2014-02-28 | 2014-06-11 | 长沙威保特环保科技有限公司 | Treatment method of low-temperature evaporation high-concentration sewage |
| CN103848464B (en) * | 2014-02-28 | 2015-12-30 | 长沙威保特环保科技有限公司 | The treatment process of low-temperature evaporation high-concentration sewage |
| CN107096248A (en) * | 2017-06-29 | 2017-08-29 | 柳健康 | One kind seven imitates tube sheet combination falling film evaporator technique |
| CN115910410A (en) * | 2023-01-04 | 2023-04-04 | 中国原子能科学研究院 | Method for treating radioactive waste liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20140910 Granted publication date: 20050907 |