CN201445833U - Defoaming equipment - Google Patents

Defoaming equipment Download PDF

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Publication number
CN201445833U
CN201445833U CN2009200424427U CN200920042442U CN201445833U CN 201445833 U CN201445833 U CN 201445833U CN 2009200424427 U CN2009200424427 U CN 2009200424427U CN 200920042442 U CN200920042442 U CN 200920042442U CN 201445833 U CN201445833 U CN 201445833U
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China
Prior art keywords
deaeration
defoaming
film
chamber
stirring
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Expired - Lifetime
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CN2009200424427U
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Chinese (zh)
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卢明立
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Individual
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Individual
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  • Degasification And Air Bubble Elimination (AREA)

Abstract

A defoaming equipment has a tank; a film rotating defoaming chamber is disposed on the upper part of the tank; a stirring defoaming chamber is disposed on the lower part of the tank; a feeding inlet and an exhaust outlet are formed on the film rotating defoaming chamber; a discharging opening is formed on the bottom of the stirring defoaming chamber; a vertical common rotating shaft is disposed in the tank; a driving mechanism connected with the rotating shaft is disposed on the top of the film rotating defoaming chamber; an umbrella shape film rotating defoaming device fixed with the rotating shaft is disposed inside the film rotating defoaming chamber; a feeding guide pipe connected with the feeding inlet is disposed on the umbrella shape film rotating defoaming device; the mouth of the feeding guide pipe is formed into flat shape; an inverted cone-shaped defoaming receiver is disposed correspondingly under the umbrella shape film rotating defoaming device; and a stirring vane is disposed inside the stirring defoaming chamber while fixed with the rotating shaft. The utility model is disposed in an equipment, can perform film defoaming, vacuum defoaming and vacuum stirring defoaming continuously; and achieves the advantages of good defoaming effect, simple operation, convenient adjustment and low cost.

Description

A kind of novel deaeration equipment
Technical field
The utility model technology relates to a kind of slurry deaeration equipment, is meant a kind of novel deaeration equipment that is used for the vicidity material especially.
Background technology
Along with the needs of development of Chinese economy and national defence, to high-performance synthetic chemistry fiber demand increasing; After particularly world wide economic crisis last year took place, China adjusted the structure of textile industry, and the development of high-performance synthetic chemistry fiber is risen to important height.
The spinning of high-performance synthetic chemistry fiber has crucial influence with the bubble amount that contains of slurry to the performance of spinning process and finished silk, and large batch of waste silk can not be carried out or occur to serious caused spinning process.And its stoste slurry is often comparatively sticky, and it is carried out relatively difficulty of deaeration; The main method that the vicidity material is used has film deaeration, vacuum defoamation, vacuum stirring deaeration etc. at present, for dropping to, the bubble amount that contains that makes slurry can satisfy spinning requirement, often adopt the repeatedly deaeration of many single equipments, this makes on the one hand, and equipment investment is more, the Operation and Maintenance expense is many, it is bigger to take up room, between individual device, have new bubble on the other hand in the convey materials process again and produce, influence the deaeration effect.
Summary of the invention
The technical problems to be solved in the utility model is at the deficiencies in the prior art, has proposed a kind of multiple deaeration operation, effective novel deaeration equipment of deaeration of carrying out continuously.
The technical problems to be solved in the utility model is achieved through the following technical solutions, a kind of novel deaeration equipment, be characterized in: be provided with a tank body, the top of tank body is for revolving film deaeration chamber, the bottom of tank body is for stirring the deaeration chamber, revolve film deaeration chamber and be provided with charging aperture and exhaust outlet, the bottom of stirring the deaeration chamber has discharging opening, in tank body, vertically be provided with a shared rotating shaft, be provided with the driving mechanism that joins with rotating shaft revolving top, film deaeration chamber, revolve the film deaerator revolving indoor being provided with of film deaeration with the fixing umbrella shape of rotating shaft, umbrella shape revolve the film deaerator above be provided with the feed conduit that is connected with charging aperture, the mouth of pipe of feed conduit is set to the shape of twitching one's mouth, the relative back taper deaeration receiver that is provided with below umbrella shape is revolved the film deaerator, and deaeration is indoor to be provided with and stirring vane that rotating shaft is fixing stirring.
The technical problems to be solved in the utility model can also come by the following technical programs further to realize that the outer wall that stirs the deaeration chamber is provided with muff heater.
The technical problems to be solved in the utility model can also come to realize that further described stirring vane is compound double-spiral structure by the following technical programs.
The technical problems to be solved in the utility model can also come to realize that further exhaust outlet is connected with vacuum suction device by the following technical programs.
The utility model compared with prior art, it makes in an equipment, carry out film deaeration, vacuum defoamation, vacuum stirring deaeration continuously, both reduced equipment investment, reduced the Operation and Maintenance expense and take up room, reduce the generation of new bubble again, make containing the bubble amount and satisfying spinning requirement of slurry.Its deaeration is effective, and is simple to operate, easy to adjust, reduces cost.
Description of drawings
Fig. 1 is a structure diagram of the present utility model.
The specific embodiment
A kind of novel deaeration equipment, be provided with a tank body, the top of tank body is for revolving film deaeration chamber 2, and the bottom of tank body revolves film deaeration chamber 2 to be provided with charging aperture and exhaust outlet 15 for stirring deaeration chamber 1, the bottom of stirring deaeration chamber 1 has discharging opening 16, vertically be provided with a shared rotating shaft 5 in tank body, be provided with the driving mechanism that joins with rotating shaft 5 revolving 2 tops, film deaeration chamber, driving mechanism comprises support and reducing motor, support 3 is located at the top of revolving film deaeration chamber 2, and reducing motor 4 is contained in the top of support 3.Rotating shaft 5 is upward through sealing device 7, and by the location of the Bearning mechanism in the support 3, the lower end is provided with aiding support 8 location.Rotating shaft 5 upper ends connect with reducing motor 4 with shaft coupling 10.
In revolving film deaeration chamber 2, be provided with the umbrella shape of fixing and revolve film deaerator 9 with rotating shaft 5, umbrella shape revolve film deaerator 9 above be provided with the feed conduit 14 that is connected with charging aperture, the mouth of pipe of feed conduit 14 is set to the shape of twitching one's mouth, the relative back taper deaeration receiver 13 that is provided with below umbrella shape is revolved film deaerator 9 is provided with in stirring deaeration chamber 1 and stirring vane 6 that rotating shaft is fixing.Stirring vane 6 adopts compound double-spiral structure.Exhaust outlet 15 is connected with vacuum suction device.
The outer wall that stirs deaeration chamber 1 is provided with muff heater 11.Muff heater 11 can adopt the heat(ing) coil structure or adopt the mode that heats with circulatory mediator in interlayer.Temperature rising, the viscosity of slurry are reduced, be convenient to improve the deaeration effect.
Slurry is imported continuously through charging aperture, flowing to the umbrella shape of rotating with rotating shaft 5 revolves on the film deaerator 9, under the effect of gravity and viscosity, diffuseed to form the fluid layer of film shape along umbrella cover, revolving the slurry that film deaerator 9 flows down from umbrella shape falls on the back taper deaeration receiver 13, form the fluid layer that has diffuseed to form the film shape along umbrella cover once more, under vacuum action, fluid has obtained the secondary deaeration and has handled.The slurry that flows down from back taper deaeration receiver 13 stirs in stirring deaeration chamber 1, and evenly degasification is extracted gas out through exhaust outlet under the effect of vacuum, and the slurry after the deaeration flows out to next procedure through discharging opening 16.

Claims (4)

1. novel deaeration equipment, it is characterized in that: be provided with a tank body, the top of tank body is for revolving film deaeration chamber, the bottom of tank body is for stirring the deaeration chamber, revolve film deaeration chamber and be provided with charging aperture and exhaust outlet, the bottom of stirring the deaeration chamber has discharging opening, in tank body, vertically be provided with a shared rotating shaft, be provided with the driving mechanism that joins with rotating shaft revolving top, film deaeration chamber, revolve the film deaerator revolving indoor being provided with of film deaeration with the fixing umbrella shape of rotating shaft, umbrella shape revolve the film deaerator above be provided with the feed conduit that is connected with charging aperture, the mouth of pipe of feed conduit is set to the shape of twitching one's mouth, the relative back taper deaeration receiver that is provided with below umbrella shape is revolved the film deaerator, deaeration is indoor to be provided with and stirring vane that rotating shaft is fixing stirring.
2. novel deaeration equipment according to claim 1 is characterized in that: the outer wall that stirs the deaeration chamber is provided with muff heater.
3. novel deaeration equipment according to claim 1 is characterized in that: described stirring vane is compound double-spiral structure.
4. novel deaeration equipment according to claim 1, it is characterized in that: exhaust outlet is connected with vacuum suction device.
CN2009200424427U 2009-06-19 2009-06-19 Defoaming equipment Expired - Lifetime CN201445833U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009200424427U CN201445833U (en) 2009-06-19 2009-06-19 Defoaming equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009200424427U CN201445833U (en) 2009-06-19 2009-06-19 Defoaming equipment

Publications (1)

Publication Number Publication Date
CN201445833U true CN201445833U (en) 2010-05-05

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009200424427U Expired - Lifetime CN201445833U (en) 2009-06-19 2009-06-19 Defoaming equipment

Country Status (1)

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CN (1) CN201445833U (en)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102021663A (en) * 2010-12-10 2011-04-20 烟台氨纶股份有限公司 Polyurethane deaeration device
CN102173061A (en) * 2010-12-20 2011-09-07 洛阳双瑞风电叶片有限公司 Liquid resin defoaming method and device for vacuum infusion forming of composite material
CN102657958A (en) * 2012-04-21 2012-09-12 深圳市汇清科技有限公司 Ultrafiltration membrane deaerating unit
CN103234574A (en) * 2013-04-24 2013-08-07 成都无极真空科技有限公司 Novel sensor vacuum filling equipment
CN103418167A (en) * 2012-05-16 2013-12-04 浙江万好万家机械有限公司 Vacuum deaeration machine for lithium battery liquid slurry
CN103845926A (en) * 2014-03-24 2014-06-11 四川兴能新材料有限公司 Defoaming equipment for eliminating foams in slurry
CN104203384A (en) * 2012-03-21 2014-12-10 株式会社夏都 Impellor of stirring device and stirring device using same
WO2015027957A1 (en) * 2013-09-02 2015-03-05 海斯摩尔生物科技有限公司 Composite defoaming method for high-viscosity pure-chitosan spinning solution
WO2015027958A3 (en) * 2013-09-02 2015-04-23 海斯摩尔生物科技有限公司 Defoaming apparatus for high-viscosity pure-chitosan spinning solution
CN105396333A (en) * 2015-12-09 2016-03-16 江阴乐圩光电股份有限公司 A vacuum defoaming machine for slurry
CN105396332A (en) * 2015-12-09 2016-03-16 江阴乐圩光电股份有限公司 A vertical defoaming machine
CN106031832A (en) * 2015-03-16 2016-10-19 山东省滕州瑞达化工有限公司 Polymer degassing apparatus
CN106626209A (en) * 2016-12-30 2017-05-10 苏州恒昇海绵机械制造有限公司 Sponge foaming machine provided with vacuum stirring device
CN107899895A (en) * 2017-12-20 2018-04-13 重庆鹏鑫达电子科技有限公司 Glue evacuation and centrifugal degassing device is used in electronics processing
WO2018161608A1 (en) * 2017-03-06 2018-09-13 京东方科技集团股份有限公司 Defoaming apparatus
CN109731371A (en) * 2019-01-16 2019-05-10 河南神马尼龙化工有限责任公司 A kind of high viscosity spinning solution continuous defoaming device and method
CN113613752A (en) * 2019-04-09 2021-11-05 M技术株式会社 Vacuum degasser with micronizing device

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102021663A (en) * 2010-12-10 2011-04-20 烟台氨纶股份有限公司 Polyurethane deaeration device
CN102173061A (en) * 2010-12-20 2011-09-07 洛阳双瑞风电叶片有限公司 Liquid resin defoaming method and device for vacuum infusion forming of composite material
CN102173061B (en) * 2010-12-20 2014-07-30 洛阳双瑞风电叶片有限公司 Liquid resin defoaming method and device for vacuum infusion forming of composite material
CN104203384A (en) * 2012-03-21 2014-12-10 株式会社夏都 Impellor of stirring device and stirring device using same
CN102657958A (en) * 2012-04-21 2012-09-12 深圳市汇清科技有限公司 Ultrafiltration membrane deaerating unit
CN102657958B (en) * 2012-04-21 2014-05-14 深圳市汇清科技有限公司 Ultrafiltration membrane deaerating unit
CN103418167B (en) * 2012-05-16 2015-06-24 浙江万好万家机械有限公司 Vacuum deaeration machine for lithium battery liquid slurry
CN103418167A (en) * 2012-05-16 2013-12-04 浙江万好万家机械有限公司 Vacuum deaeration machine for lithium battery liquid slurry
CN103234574A (en) * 2013-04-24 2013-08-07 成都无极真空科技有限公司 Novel sensor vacuum filling equipment
WO2015027957A1 (en) * 2013-09-02 2015-03-05 海斯摩尔生物科技有限公司 Composite defoaming method for high-viscosity pure-chitosan spinning solution
WO2015027958A3 (en) * 2013-09-02 2015-04-23 海斯摩尔生物科技有限公司 Defoaming apparatus for high-viscosity pure-chitosan spinning solution
CN103845926A (en) * 2014-03-24 2014-06-11 四川兴能新材料有限公司 Defoaming equipment for eliminating foams in slurry
CN106031832A (en) * 2015-03-16 2016-10-19 山东省滕州瑞达化工有限公司 Polymer degassing apparatus
CN106031832B (en) * 2015-03-16 2021-03-16 山东省滕州瑞达化工有限公司 Polymer degassing device
CN105396333A (en) * 2015-12-09 2016-03-16 江阴乐圩光电股份有限公司 A vacuum defoaming machine for slurry
CN105396332A (en) * 2015-12-09 2016-03-16 江阴乐圩光电股份有限公司 A vertical defoaming machine
CN106626209A (en) * 2016-12-30 2017-05-10 苏州恒昇海绵机械制造有限公司 Sponge foaming machine provided with vacuum stirring device
WO2018161608A1 (en) * 2017-03-06 2018-09-13 京东方科技集团股份有限公司 Defoaming apparatus
CN108525351A (en) * 2017-03-06 2018-09-14 京东方科技集团股份有限公司 A kind of defoaming device
US10926198B2 (en) 2017-03-06 2021-02-23 Boe Technology Group Co., Ltd. Deaeration apparatus
CN107899895A (en) * 2017-12-20 2018-04-13 重庆鹏鑫达电子科技有限公司 Glue evacuation and centrifugal degassing device is used in electronics processing
CN109731371A (en) * 2019-01-16 2019-05-10 河南神马尼龙化工有限责任公司 A kind of high viscosity spinning solution continuous defoaming device and method
CN109731371B (en) * 2019-01-16 2021-03-23 河南神马尼龙化工有限责任公司 Continuous defoaming device and method for high-viscosity spinning solution
CN113613752A (en) * 2019-04-09 2021-11-05 M技术株式会社 Vacuum degasser with micronizing device
US20220203267A1 (en) * 2019-04-09 2022-06-30 M. Technique Co., Ltd. Vacuum deaerator equipped with refining device

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GR01 Patent grant
CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20100505