CN203861937U - Horizontal spraying-film evaporator - Google Patents

Horizontal spraying-film evaporator Download PDF

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Publication number
CN203861937U
CN203861937U CN201420121902.6U CN201420121902U CN203861937U CN 203861937 U CN203861937 U CN 203861937U CN 201420121902 U CN201420121902 U CN 201420121902U CN 203861937 U CN203861937 U CN 203861937U
Authority
CN
China
Prior art keywords
heating tube
group
tube group
housing
steam
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201420121902.6U
Other languages
Chinese (zh)
Inventor
牛量
云泽国
李东
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tianjin Hengmai Electromechanical Technology Co Ltd
Original Assignee
Tianjin Hengmai Electromechanical Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tianjin Hengmai Electromechanical Technology Co Ltd filed Critical Tianjin Hengmai Electromechanical Technology Co Ltd
Priority to CN201420121902.6U priority Critical patent/CN203861937U/en
Application granted granted Critical
Publication of CN203861937U publication Critical patent/CN203861937U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a horizontal spraying-film evaporator. The horizontal spraying-film evaporator comprises a horizontal case, a heating tube group and a support base, wherein two ends of the heating tube group are installed in the case respectively through tube plates, the support base is installed on the outer side of the case, one end of the heating tube group is installed on a steam chamber at one end of the case in a communicated manner, a steam inlet pipe is manufactured on the steam chamber, the other end of the heating tube group is installed on a water tank at the other end of the case in a communicated manner, a condensate water outlet is installed at the lower part of the water tank, a group of spraying pipes which are parallel with the heating tube group are installed at the upper part in the case, red liquor inlets are arranged at middle parts of the spraying pipes in the group, nozzles are installed at lower parts of the spraying pipes in the group at intervals, a steam outlet is manufactured at the top of the case, and a concentrated red liquor outlet is manufactured at the bottom of the case. The horizontal spraying-film evaporator adopts a horizontal spraying-film method and is high in heat exchange efficiency; heating steam passes through the tube pass, so that the required medium amount is small, the energy consumption is low, and the outside of the heating tube group is easy to clean after scaling.

Description

A kind of horizontal spray film evaporator
Technical field
The utility model belongs to paper making equipment field, particularly a kind of horizontal spray film evaporator.
Background technology
The red liquid of acid polishing has that concentration is high, the feature of easy fouling, and traditional tubular type or plate-type evaporator not only heat transfer efficiency are low, and after fouling of evaporator, cleaning is more difficult.Existing horizontal-type evaporator is generally horizontal shell and tube flooded evaporator, when for papermaking red liquid evaporation and concentration, it typically is heat medium and walks shell side, papermaking red liquid is walked tube side, and its existence needs heat transferring medium amount many, and energy consumption is high, and in tube bank, easily fouling, clears up difficult problem.Existing plate-type evaporator, when being applied to red liquid evaporation and concentration, adopts falling liquid film mode conventionally, has the problem that heat transfer efficiency is low.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, provides a kind of heat transfer efficiency high, and energy consumption is little, is easy to the horizontal spray film evaporator of cleaning.
The utility model solves its technical problem and is achieved through the following technical solutions:
A kind of horizontal spray film evaporator, comprise horizontal housing, heating tube group, supporting seat, heating tube group two ends are installed in housing by tube sheet respectively, hull outside is provided with supporting seat, it is characterized in that: the common vaporium that is installed on shell end that is communicated with in one end of described heating tube group, this vaporium is shaped with steam inlet pipe, the common water tank that is installed on the housing other end that is communicated with of the other end of heating tube group, and water tank bottom is provided with condensation-water drain; Top in housing is provided with the one group of shower that is parallel to described heating tube group, the middle part of this group of shower is provided with red liquid inlet, the equal interval, bottom of this group of shower is provided with one group of nozzle, top at housing is shaped with steam (vapor) outlet, is shaped with concentrated red liquid outlet in the bottom of housing.
And, the demister that is positioned at steam (vapor) outlet bottom is installed in described housing.
And, described nozzle consists of nozzle body and water conservancy diversion bolt, nozzle body consists of inlet, main body and liquid outlet, liquid outlet diameter is less than inlet diameter, water conservancy diversion bolt is installed in the main body of nozzle body, this water conservancy diversion bolt consists of newel and two flow deflectors, is shaped with guiding gutter on flow deflector, and this flow deflector and newel are 50-70 degree.
Advantage of the present utility model and beneficial effect are:
1, this horizontal spray film evaporator, red liquid enters evaporator shell by shower, evenly spray is to the upper liquid film that forms of the superiors' pipe of heating tube group, liquid film produces heat exchange with the interior steam of pipe, thereby lower boiling part water in red liquid is undergone phase transition and become steam, and the liquid not undergoing phase transition pools drop and drops onto on lower one deck heating tube in heating tube bottom, and drop when heating tube upside moves downward, can on heating tube outer wall, form liquid film and with pipe in steam generation heat exchange, repeat the heat exchanging process of ground floor pipe until fluid drips drops out heating tube group, steam enters heating tube group by vaporium and with the outer red liquid heat exchange of pipe and be condensed into water, condensed water is pooled in the water tank of right side and sends, water in red liquid undergoes phase transition the secondary steam of generation and is sent by the road by case top steam.
2, this horizontal spray film evaporator, adopts one group of nozzle consisting of nozzle body and water conservancy diversion bolt, and body enters the water conservancy diversion bolt of first flowing through after nozzle body, through water conservancy diversion bolt effect liquid, becomes rotation status; The liquid of rotation forms uniform circular distribution face by the bottom ejection of nozzle body; And because the outlet at bottom of nozzle body is little compared with nozzle body import, therefore liquid locates to obtain higher flow velocity again, make the liquid of ejection present spray pattern; And can there is flash distillation in the very first time in the atomized liquid spraying through nozzle, the part water in the much more popular liquid of band, a booster action to red liquid evaporation; Red liquid through nozzle ejection is uniform circle, and cloth liquid is even, and the efficiency of evaporimeter is improved a lot.
3, the utility model scientific structure design is reasonable, adopts horizontal spray film mode, makes red liquid realize full flashing when entering evaporimeter inside, and then carries out falling film evaporation, and heat exchange efficiency is high; Tube side is walked in heating steam, and required medium amount is little, and energy consumption is low, after the outside fouling of heating tube group, is easy to cleaning, is a kind of horizontal spray film evaporator with higher innovation.
Accompanying drawing explanation
Fig. 1 is system architecture schematic diagram of the present utility model;
Fig. 2 is the right view of Fig. 1;
Fig. 3 is the structural representation of nozzle of the present utility model;
Fig. 4 is the right view of Fig. 3;
Fig. 5 is the structural representation of water conservancy diversion bolt in Fig. 3;
Fig. 6 is the left view of Fig. 5;
Fig. 7 is the perspective view of water conservancy diversion bolt.
Description of reference numerals:
1-steam inlet pipe, 2-housing, 3-heating tube group, 4-demister, 5-steam (vapor) outlet, the red liquid inlet of 6-, 7-shower, 8-nozzle, 9-manhole, 10-water tank, 11-condensation-water drain, the concentrated red liquid outlet of 12-, 13-supporting seat, 14-vaporium, 15-inlet, 16-water conservancy diversion bolt, 17-main body, 18-liquid outlet, 19-primary screw, 20-newel, 21-flow deflector, 22-guiding gutter.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail, and following examples are descriptive, is not determinate, can not limit protection domain of the present utility model with this.
A horizontal spray film evaporator, comprises horizontal housing 2, heating tube group 3, supporting seat 13, and heating tube group two ends are installed in housing by tube sheet respectively, and hull outside is provided with supporting seat.Its innovation is: the common vaporium 14 that is installed on shell end that is communicated with in one end of heating tube group, this vaporium is shaped with steam inlet pipe 1, the common water tank 10 that is installed on the housing other end that is communicated with of the other end of heating tube group, water tank bottom is provided with condensation-water drain 11; Top in housing is provided with the one group of shower 7 that is parallel to described heating tube group, and the middle part of this group of shower is provided with red liquid inlet 6, and the equal interval, bottom of this group of shower is provided with one group of nozzle 8.In the present embodiment, be provided with and be arranged with four showers in parallel, every shower is provided with 8 nozzles, to guarantee the uniformity of spraying.At the top of housing, be shaped with steam (vapor) outlet 5, in the bottom of housing, be shaped with concentrated red liquid outlet 12.The demister 4 that is positioned at steam (vapor) outlet bottom is installed in housing.Shell end is provided with manhole 9, for clearing up maintenance.
Nozzle consists of nozzle body and water conservancy diversion bolt 16, and nozzle body consists of inlet 15, main body 17 and liquid outlet 18, and liquid outlet diameter is less than inlet diameter, and liquid outlet diameter is 0.4~0.5 of inlet diameter.Water conservancy diversion bolt is installed in the main body of nozzle body, and this water conservancy diversion bolt consists of newel 20 and two flow deflectors 21, is shaped with guiding gutter 22 on flow deflector, and this flow deflector and newel are 50-70 degree.Water conservancy diversion bolt and nozzle body main diameter adopt a primary screw 19 to be fixed installation.Through water conservancy diversion bolt effect liquid, become rotation status; The liquid of rotation forms uniform circular distribution face by the bottom ejection of nozzle body; And because the outlet at bottom of nozzle body is little compared with nozzle body import, therefore liquid locates to obtain higher flow velocity again, make the liquid of ejection present spray pattern.
The operation principle of this horizontal spray film evaporator is:
Red liquid enters evaporator shell by shower, evenly spray is to the upper liquid film that forms of the superiors' pipe of heating tube group, liquid film produces heat exchange with the interior steam of pipe, thereby lower boiling part water in red liquid is undergone phase transition and become steam, and the liquid not undergoing phase transition pools drop and drops onto on lower one deck heating tube in heating tube bottom, and drop when heating tube upside moves downward, can on heating tube outer wall, form liquid film and with pipe in steam generation heat exchange, repeat the heat exchanging process of ground floor pipe until fluid drips drops out heating tube group; Steam enters heating tube group by vaporium and with the outer red liquid heat exchange of pipe and be condensed into water, condensed water is pooled in the water tank of right side and sends; Water in red liquid undergoes phase transition the secondary steam of generation and is sent by the road by case top steam.
Although disclosed embodiment of the present utility model and accompanying drawing for the purpose of illustration, but it will be appreciated by those skilled in the art that, within not departing from the spirit and scope of the utility model and claims, various replacements, variation and modification are all possible, and therefore scope of the present utility model is not limited to embodiment and the disclosed content of accompanying drawing.

Claims (3)

1. a horizontal spray film evaporator, comprise horizontal housing, heating tube group, supporting seat, heating tube group two ends are installed in housing by tube sheet respectively, hull outside is provided with supporting seat, it is characterized in that: the common vaporium that is installed on shell end that is communicated with in one end of described heating tube group, this vaporium is shaped with steam inlet pipe, the common water tank that is installed on the housing other end that is communicated with of the other end of heating tube group, and water tank bottom is provided with condensation-water drain; Top in housing is provided with the one group of shower that is parallel to described heating tube group, the middle part of this group of shower is provided with red liquid inlet, the equal interval, bottom of this group of shower is provided with one group of nozzle, top at housing is shaped with steam (vapor) outlet, is shaped with concentrated red liquid outlet in the bottom of housing.
2. horizontal spray film evaporator according to claim 1, is characterized in that: the demister that is positioned at steam (vapor) outlet bottom is installed in described housing.
3. horizontal spray film evaporator according to claim 1, it is characterized in that: described nozzle consists of nozzle body and water conservancy diversion bolt, nozzle body consists of inlet, main body and liquid outlet, liquid outlet diameter is less than inlet diameter, water conservancy diversion bolt is installed in the main body of nozzle body, this water conservancy diversion bolt consists of newel and two flow deflectors, is shaped with guiding gutter on flow deflector, and this flow deflector and newel are 50-70 degree.
CN201420121902.6U 2014-03-18 2014-03-18 Horizontal spraying-film evaporator Expired - Fee Related CN203861937U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420121902.6U CN203861937U (en) 2014-03-18 2014-03-18 Horizontal spraying-film evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420121902.6U CN203861937U (en) 2014-03-18 2014-03-18 Horizontal spraying-film evaporator

Publications (1)

Publication Number Publication Date
CN203861937U true CN203861937U (en) 2014-10-08

Family

ID=51642928

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420121902.6U Expired - Fee Related CN203861937U (en) 2014-03-18 2014-03-18 Horizontal spraying-film evaporator

Country Status (1)

Country Link
CN (1) CN203861937U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105923868A (en) * 2016-03-15 2016-09-07 金能科技股份有限公司 Coking wastewater depth treatment process and processing system
CN108027134A (en) * 2015-07-07 2018-05-11 获劳动红旗勋章和Czsr劳动勋章的水压试验设计院联合股份公司 Steam generator
CN110314396A (en) * 2019-07-23 2019-10-11 广东闻扬环境科技有限公司 Lying pipe falling film evaporator

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108027134A (en) * 2015-07-07 2018-05-11 获劳动红旗勋章和Czsr劳动勋章的水压试验设计院联合股份公司 Steam generator
CN105923868A (en) * 2016-03-15 2016-09-07 金能科技股份有限公司 Coking wastewater depth treatment process and processing system
CN105923868B (en) * 2016-03-15 2019-01-04 金能科技股份有限公司 A kind of advanced treatment process of coking waste water and its processing system
CN110314396A (en) * 2019-07-23 2019-10-11 广东闻扬环境科技有限公司 Lying pipe falling film evaporator

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20141008

Termination date: 20190318