CN204100560U - Efficient degreasing bath heater - Google Patents

Efficient degreasing bath heater Download PDF

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Publication number
CN204100560U
CN204100560U CN201420077814.0U CN201420077814U CN204100560U CN 204100560 U CN204100560 U CN 204100560U CN 201420077814 U CN201420077814 U CN 201420077814U CN 204100560 U CN204100560 U CN 204100560U
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CN
China
Prior art keywords
degreasing
heat exchanger
degreasing bath
secondary groove
major trough
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
CN201420077814.0U
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Chinese (zh)
Inventor
邢礼宏
毛崇江
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.)
YANCHENG DONGFANG TIANCHENG MACHINERY CO Ltd
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YANCHENG DONGFANG TIANCHENG MACHINERY CO Ltd
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Priority to CN201420077814.0U priority Critical patent/CN204100560U/en
Application granted granted Critical
Publication of CN204100560U publication Critical patent/CN204100560U/en
Anticipated expiration legal-status Critical
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00Climate change mitigation technologies for sector-wide applications
    • Y02P80/10Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The utility model discloses a kind of efficient degreasing bath heater, described heater comprises degreasing bath, degreasing heat exchanger and degreaser circulating pump, described degreasing bath comprises major trough and secondary groove, described degreasing heat exchanger is arranged on the bottom of secondary groove, demarcation strip is provided with between described secondary groove and major trough, described demarcation strip top is major and minor tank liquor UNICOM mouth, the bottom of described secondary groove is connected with degreaser circulating pump by connecting line, and described degreaser circulating pump is provided with on the bottom and end sidewalls that multiple tracks infusion pipeline is connected to major trough; Degreasing bath heat exchanger is directly placed in the secondary groove structure of degreasing bath by the utility model, and by being connected with major trough, the tank liquor of degreasing bath carries out heat transmission by direct contact heat exchanger wall, and the overall efficiency of heating surface can reach 90%-95%; What whole circulating heat exchange system can be succinct simultaneously is arranged on Pretreatment Line, has both reduced the device space and has taken, reduced equipment investment again.

Description

Efficient degreasing bath heater
Technical field
The utility model relates to the production equipment field of paint line, particularly relate to a kind of can the device of high-efficiency heating degreasing bath tank liquor.
Background technology
All require to carry out degreasing operation to workpiece in enormous quantities, high-quality manufacturing technique for painting dressing at present, and the degreasing bath applied in degreasing operation generally adopts the principle of secondary heat exchange to heat, concrete method of operating is as follows: first heated the water in hot water storgae by heat exchanger, hot water after heating is transported to after on plate type heat exchanger by hot water circulating pump and gets back in hot water storgae by circulating line the circulating-heating realizing hot water, and degreaser is also transported to after on plate type heat exchanger through degreaser circulating pump and is back on degreasing bath through circulation line, and then the tank liquor circulating-heating (as shown in Figure 1) completed in degreasing bath, need in whole heating process through secondary heat exchange, the overall efficiency of heating surface is lower, adding thermogenetic heat has major part to be lost in heat exchanging process, the efficiency of heating surface can only reach 60%-70%.
Utility model content
For above-mentioned Problems existing, it is high that the utility model object is to provide a kind of efficiency of heating surface, structure simple degreasing bath tank liquor heater.
In order to achieve the above object, the technical solution adopted in the utility model is as follows: a kind of efficient degreasing bath heater, described heater comprises degreasing bath, degreasing heat exchanger and degreaser circulating pump, described degreasing bath comprises major trough and secondary groove, described degreasing heat exchanger is arranged on the bottom of secondary groove, demarcation strip is provided with between described secondary groove and major trough, described demarcation strip top is main, secondary tank liquor UNICOM mouth, the bottom of described secondary groove is connected with degreaser circulating pump by connecting line, described degreaser circulating pump is provided with on the bottom and end sidewalls that multiple tracks infusion pipeline is connected to major trough.
Improve as one of the present utility model, the top of described degreasing heat exchanger is provided with many flue gas pipes of evenly arranging, and flue gas pipe is many return structures, to improve the heat utilization efficiency of flue gas; Bottom is provided with circular combustion chamber, and one end of described circular combustion chamber is connected on burner for heating, and the other end is connected on flue gas pipe, and the outlet side of described flue gas pipe is connected on smoke discharging pipe; The utility model mainly directly to be contacted with tank liquor by the housing of degreasing heat exchanger and carries out heat transmission, the circular combustion chamber of degreasing heat exchanger produces a large amount of heats in combustion, after a part passes to tank liquor, another part is easily diffused into outside system by flue gas, therefore contacted with the further of tank liquor by many backhauls flue gas heating tube, expand heat exchange contact area and extend heat exchanger time, improving the efficiency of heating surface.
Improve as one of the present utility model, in the bottom that described infusion pipeline is evenly distributed on major trough and end sidewalls, every root infusion pipeline is equipped with by-pass valve control, spacing between two adjacent infusion pipelines is 80-100cm, by infusion pipeline, the uniform liquid heated is transported in degreasing bath, equally distributed infusion pipeline, in order to ensure that in degreasing bath, each reaction zone temperature is homogeneous, improves degreasing reaction efficiency.
Improve as one of the present utility model, the height of described demarcation strip is higher than the top 20-40cm of degreasing heat exchanger, by major trough and the secondary groove of divides degreasing bath, both ensure that degreasing heat exchanger was immersed in tank liquor completely, ensure again the directed flow of tank liquor, increase the uniformity of heat conductive contact time and tank liquor heating, improve the overall efficiency of heating surface.
The utility model has the advantage of: degreasing bath heat exchanger is directly placed in the secondary groove structure of degreasing bath by the utility model, by being connected with major trough, the tank liquor of degreasing bath carries out heat transmission by direct contact heat exchanger wall, and the overall efficiency of heating surface can reach 90%-95%; What whole circulating heat exchange system can be succinct simultaneously is arranged on Pretreatment Line, has both reduced the device space and has taken, reduced equipment investment again.
Accompanying drawing explanation
Fig. 1 is former degreasing bath heater structure diagram;
Fig. 2 is the utility model structure diagram;
Fig. 3 is the utility model degreasing heat exchanger syndeton sketch;
Fig. 4 is the utility model degreasing heat exchanger cross-sectional;
Wherein, 1 degreasing bath major trough, the secondary groove of 2 degreasing baths, 3 degreasing heat exchangers, the circular combustion chamber of 3-1,3-2 flue gas pipe, 4 demarcation strips, 5 degreaser circulating pumps, 6 infusion pipelines, 7 reaction pipelines, 8 sample taps, 9 reactors, 10 burner for heating, 11 smoke discharging pipes.
Detailed description of the invention
Illustrate below in conjunction with accompanying drawing and with detailed description of the invention, the utility model to be described in further detail.
embodiment 1:the efficient degreasing bath heater of one as shown in Figure 2, described heater comprises degreasing bath 1 and 2, degreasing heat exchanger 3 and degreaser circulating pump 5, described degreasing bath comprises major trough 1 and secondary groove 2, described degreasing heat exchanger 3 is arranged on the bottom of secondary groove 2, demarcation strip 4 is provided with between described secondary groove 2 and major trough 1, the top of described demarcation strip 4 is main, secondary tank liquor UNICOM mouth, the bottom of described secondary groove 2 is connected with degreaser circulating pump 5 by connecting line, described degreaser circulating pump 5 is provided with on the bottom and end sidewalls that multiple tracks infusion pipeline 6 is connected to major trough 1.
embodiment 2:as shown in Figure 2,3, 4, the top of described degreasing heat exchanger 3 is provided with the many flue gas pipe 3-2 evenly arranged, and flue gas pipe is many return structures 3-2, to improve the heat utilization efficiency of flue gas, bottom is provided with circular combustion chamber 3-1, one end of described circular combustion chamber 3-1 is connected on burner for heating 10, and the other end is connected on flue gas pipe 3-2, and the outlet side of described flue gas pipe 3-2 is connected on smoke discharging pipe 11; The utility model mainly directly to be contacted with tank liquor by the housing of degreasing heat exchanger 3 and carries out heat transmission, the circular combustion chamber 3-1 of degreasing heat exchanger produces a large amount of heats in combustion, after a part passes to tank liquor, another part is easily diffused into outside system by flue gas, therefore contacted with the further of tank liquor by many backhauls flue gas heating tube, expand heat exchange contact area and extend heat exchanger time, improving the efficiency of heating surface.
embodiment 3:as shown in Figure 2, in the bottom that described infusion pipeline 6 is evenly distributed on major trough 1 and end sidewalls, every root infusion pipeline is equipped with by-pass valve control, spacing between two adjacent infusion pipelines is 60-70cm, by infusion pipeline, the uniform liquid heated is transported in degreasing bath, equally distributed infusion pipeline, in order to ensure that in degreasing bath, each reaction zone temperature is homogeneous, improves degreasing reaction efficiency.
embodiment 4:as shown in Figure 2, the height of described demarcation strip 4 is higher than the top 20-40cm of degreasing heat exchanger 3, major trough 1 and the secondary groove 2 of degreasing bath is separated by demarcation strip 4, both ensure that degreasing heat exchanger 3 was immersed in tank liquor completely, ensure again the directed flow of tank liquor, increase the uniformity of heat conductive contact time and tank liquor heating, improve the overall efficiency of heating surface.
embodiment 5:as shown in Figure 2, described degreaser circulating pump 5 is connected on reactor 9 and sample tap 8 through the pipeline 7 that responds; Tank liquor can be done further operation by the reaction pipeline of parallel connection, form overall technological process production line, improve the production efficiency of entire plant.
It should be noted that, above-mentioned is only preferred embodiment of the present utility model, is not used for limiting protection domain of the present utility model, and equivalents done on the basis of above-described embodiment all belongs to protection domain of the present utility model.

Claims (4)

1. an efficient degreasing bath heater, described heater comprises degreasing bath, degreasing heat exchanger and degreaser circulating pump, described degreasing bath comprises major trough and secondary groove, it is characterized in that, described degreasing heat exchanger is arranged on the bottom of secondary groove, demarcation strip is provided with between described secondary groove and major trough, described demarcation strip top is major and minor tank liquor UNICOM mouth, the bottom of described secondary groove is connected with degreaser circulating pump by connecting line, and described degreaser circulating pump is provided with on the bottom and end sidewalls that multiple tracks infusion pipeline is connected to major trough.
2. efficient degreasing bath heater according to claim 1, is characterized in that, the top of described degreasing heat exchanger is provided with many flue gas pipes of evenly arranging, and described flue gas pipe is many return structures; Bottom is provided with circular combustion chamber, and one end of described circular combustion chamber is connected on burner for heating, and the other end is connected on flue gas pipe, and the outlet side of described flue gas pipe is connected on smoke discharging pipe.
3. efficient degreasing bath heater according to claim 1, it is characterized in that, in the bottom that described infusion pipeline is evenly distributed on major trough and end sidewalls, every root infusion pipeline is equipped with by-pass valve control, and the spacing between two adjacent infusion pipelines is 80-100cm.
4. efficient degreasing bath heater according to claim 1, is characterized in that, the height of described demarcation strip is higher than the top 20-40cm of degreasing heat exchanger.
CN201420077814.0U 2014-02-24 2014-02-24 Efficient degreasing bath heater Expired - Fee Related CN204100560U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420077814.0U CN204100560U (en) 2014-02-24 2014-02-24 Efficient degreasing bath heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420077814.0U CN204100560U (en) 2014-02-24 2014-02-24 Efficient degreasing bath heater

Publications (1)

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CN204100560U true CN204100560U (en) 2015-01-14

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104879915A (en) * 2015-05-21 2015-09-02 安徽省安庆市汉城电子通讯有限公司 Degreasing tank heating system
CN109539770A (en) * 2018-12-28 2019-03-29 太仓联洲机械设备有限公司 A kind of baking oven Waste Heat Recovery System
CN110528011A (en) * 2019-08-29 2019-12-03 四川中豪科技有限公司 A kind of aluminium alloy extrusions degreasing bath and degreasing process
CN113526612A (en) * 2021-05-31 2021-10-22 东风商用车有限公司 Degreasing agent oil stain separation regeneration device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104879915A (en) * 2015-05-21 2015-09-02 安徽省安庆市汉城电子通讯有限公司 Degreasing tank heating system
CN109539770A (en) * 2018-12-28 2019-03-29 太仓联洲机械设备有限公司 A kind of baking oven Waste Heat Recovery System
CN110528011A (en) * 2019-08-29 2019-12-03 四川中豪科技有限公司 A kind of aluminium alloy extrusions degreasing bath and degreasing process
CN113526612A (en) * 2021-05-31 2021-10-22 东风商用车有限公司 Degreasing agent oil stain separation regeneration device
CN113526612B (en) * 2021-05-31 2022-05-03 东风商用车有限公司 Degreasing agent separation greasy dirt regenerating unit

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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

Granted publication date: 20150114

Termination date: 20200224

CF01 Termination of patent right due to non-payment of annual fee