CN204275819U - A kind of ultrafiltration apparatus for soy sauce, vinegar - Google Patents
A kind of ultrafiltration apparatus for soy sauce, vinegar Download PDFInfo
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- CN204275819U CN204275819U CN201420695514.9U CN201420695514U CN204275819U CN 204275819 U CN204275819 U CN 204275819U CN 201420695514 U CN201420695514 U CN 201420695514U CN 204275819 U CN204275819 U CN 204275819U
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- 235000013555 soy sauce Nutrition 0.000 title claims abstract description 22
- 235000021419 vinegar Nutrition 0.000 title claims abstract description 22
- 239000000052 vinegar Substances 0.000 title claims abstract description 22
- 238000000108 ultra-filtration Methods 0.000 title claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 100
- 239000012528 membrane Substances 0.000 claims abstract description 32
- 238000001471 micro-filtration Methods 0.000 claims abstract description 26
- 239000000571 coke Substances 0.000 claims abstract description 24
- 238000001914 filtration Methods 0.000 claims abstract description 21
- 239000012510 hollow fiber Substances 0.000 claims abstract description 15
- 239000000463 material Substances 0.000 claims abstract description 9
- 238000001179 sorption measurement Methods 0.000 claims description 20
- 239000010865 sewage Substances 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 239000000565 sealant Substances 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 3
- 229920002492 poly(sulfone) Polymers 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 238000001223 reverse osmosis Methods 0.000 claims description 3
- 230000003068 static effect Effects 0.000 claims description 2
- 239000011550 stock solution Substances 0.000 claims 3
- 239000003292 glue Substances 0.000 claims 1
- 238000012856 packing Methods 0.000 claims 1
- 238000001556 precipitation Methods 0.000 abstract description 5
- 230000007774 longterm Effects 0.000 abstract description 3
- 239000012535 impurity Substances 0.000 description 5
- 235000013409 condiments Nutrition 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
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- Soy Sauces And Products Related Thereto (AREA)
Abstract
本实用新型公开了一种用于酱油、醋的超滤设备,其包括:前级的活性焦吸附器和二级的超微滤膜过滤器;活性焦吸附器的清液出口通过连接管与超微滤膜过滤器的进液口相连通;超微滤膜过滤器内设置有过滤区,该过滤区内的过滤材料为若干根n型结构的中空纤维,该n型结构下部的两个开口端均用于向外导出酱油或醋的纯净液,纯净液经净液出口导出;未被滤出的酱油或醋经循环出口及管路返回到所述进液口。通过超微过滤后的酱油或醋清澈透明,长久放置也不会出现沉淀,并且通过循环过滤最大限度地降低了过滤过程中的产品损耗,即在过滤环节产品损耗不到1%。
The utility model discloses an ultrafiltration device for soy sauce and vinegar, which comprises: a front-stage active coke adsorber and a second-stage ultra-microfiltration membrane filter; the clear liquid outlet of the active coke adsorber is connected to the The liquid inlets of the ultra-microfiltration membrane filter are connected; the ultra-microfiltration membrane filter is provided with a filtering area, and the filtering material in the filtering area is a plurality of hollow fibers of n-type structure, and the two lower parts of the n-type structure are The open ends are all used to lead out the pure liquid of soy sauce or vinegar, and the pure liquid is exported through the clean liquid outlet; the unfiltered soy sauce or vinegar returns to the liquid inlet through the circulation outlet and the pipeline. The soy sauce or vinegar after ultra-micro filtration is clear and transparent, and there will be no precipitation after long-term storage, and the product loss in the filtration process is minimized by circulating filtration, that is, the product loss in the filtration process is less than 1%.
Description
技术领域 technical field
本实用新型涉及到一种用于过滤酱油、醋中杂质的超滤设备。 The utility model relates to an ultrafiltration device for filtering impurities in soy sauce and vinegar.
背景技术 Background technique
酱油、醋是人们日常生活中所必须的调味品,在制作过程中,难免会有残渣无法通过简单的沉淀和过滤去除掉,由此,在现有的瓶装或桶装产品中,经常存在黑色沉淀物存在,在烹饪时影响菜肴的色泽和味道。 Soy sauce and vinegar are necessary condiments in people's daily life. During the production process, there will inevitably be residues that cannot be removed by simple precipitation and filtration. Therefore, in the existing bottled or barreled products, there are often black Precipitation exists and affects the color and taste of dishes during cooking.
实用新型内容 Utility model content
为解决上述问题,本实用新型的目的在于提供一种将酱油、醋中的杂质去除的超滤设备。通过该设备过滤后的产品质量损失少,但成品色泽清澈透明,长时间放置后无沉淀。 In order to solve the above problems, the purpose of this utility model is to provide an ultrafiltration device for removing impurities in soy sauce and vinegar. The quality loss of the product filtered by this equipment is small, but the color of the finished product is clear and transparent, and there is no precipitation after long-term storage.
为实现上述目的,本实用新型一种用于酱油、醋的超滤设备包括:前级的活性焦吸附器和二级的超微滤膜过滤器;所述超微滤膜过滤器设置有进液口、循环出口和净液出口;活性焦吸附器设置有原液进口、排污口和清液出口,活性焦吸附器的清液出口通过连接管与超微滤膜过滤器的进液口相连通;超微滤膜过滤器内设置有过滤区,该过滤区内的过滤材料为若干根n型结构的中空纤维,该n型结构下部的两个开口端均用于向外导出酱油或醋的纯净液,纯净液经所述净液出口导出;未被滤出的酱油或醋经循环出口及管路返回到所述进液口。 In order to achieve the above object, a kind of ultrafiltration equipment used for soy sauce and vinegar of the present utility model comprises: the active coke adsorber of preceding stage and the ultramicrofiltration membrane filter of secondary stage; Described ultramicrofiltration membrane filter is provided with advanced Liquid port, circulation outlet and net liquid outlet; the active coke adsorber is provided with raw liquid inlet, sewage outlet and clear liquid outlet, and the clear liquid outlet of the active coke adsorber is connected with the liquid inlet of the ultra-microfiltration membrane filter through a connecting pipe ; The ultra-microfiltration membrane filter is provided with a filter area, and the filter material in the filter area is a plurality of hollow fibers of n-type structure, and the two open ends of the bottom of the n-type structure are used to lead out soy sauce or vinegar. Pure liquid, the pure liquid is exported through the clean liquid outlet; unfiltered soy sauce or vinegar is returned to the liquid inlet through the circulation outlet and the pipeline.
进一步,所述循环出口处设置有压力控制阀;所述进液口处设置有液体输送泵,所述未被滤出的酱油或醋经液体输送泵返回到所述超微滤膜过滤器内进行循环过滤。所述活性焦吸附器的清液出口依次通过连接管、所述液体输送泵与超微滤膜过滤器的进液口连接。 Further, a pressure control valve is provided at the circulation outlet; a liquid delivery pump is provided at the liquid inlet, and the unfiltered soy sauce or vinegar is returned to the ultra-microfiltration membrane filter through the liquid delivery pump Perform cycle filtration. The clear liquid outlet of the activated coke adsorber is sequentially connected to the liquid inlet of the ultra-microfiltration membrane filter through a connecting pipe and the liquid delivery pump.
进一步,所述中空纤维的材料为聚砜,其外径为400±20μm,内径为250±20μm;所述中空纤维的超微滤膜微孔孔径为0.07-0.08μm。 Further, the material of the hollow fiber is polysulfone, its outer diameter is 400±20 μm, and its inner diameter is 250±20 μm; the pore diameter of the ultramicrofiltration membrane of the hollow fiber is 0.07-0.08 μm.
进一步,所述活性焦吸附器内自下而上设置有污液区、吸附区和清液区,吸附区内的吸附材料为颗粒度为ф10-15mm活性焦,活性焦厚度不小于700mm;污液区与所述吸附区中间设置有下隔膜,清液区与所述吸附区中间设置有上隔膜。 Further, the activated coke adsorber is provided with a dirty liquid area, an adsorption area and a clear liquid area from bottom to top, the adsorption material in the adsorption area is active coke with a particle size of ф10-15mm, and the thickness of the active coke is not less than 700mm; A lower diaphragm is arranged between the liquid region and the adsorption region, and an upper diaphragm is arranged between the clear liquid region and the adsorption region.
进一步,待净化处理的原液通过所述原液进口进入所述污液区,原液在液压或前级储液池的静压下,或水泵压力下,自下而上逆渗透通过所述吸附区进入所述清液区,原液经吸附处理后变成清液,清液经清液出口流出,污液区内的污液或杂质可通过排污口排出。 Further, the raw liquid to be purified enters the dirty liquid area through the raw liquid inlet, and the raw liquid enters through the adsorption area through reverse osmosis from bottom to top under the hydraulic pressure or the static pressure of the pre-stage liquid storage tank, or the pressure of the water pump. In the clear liquid area, the raw liquid becomes clear liquid after adsorption treatment, and the clear liquid flows out through the clear liquid outlet, and the dirty liquid or impurities in the dirty liquid area can be discharged through the sewage outlet.
进一步,所述活性焦吸附器的原液进口和清液出口设置在清液区的上部,原液通过原液进口及引水管进入污液区,所述排污口设置在所述污液区的底部。 Further, the raw liquid inlet and the clear liquid outlet of the active coke adsorber are arranged at the upper part of the clear liquid area, the raw liquid enters the dirty liquid area through the raw liquid inlet and the water diversion pipe, and the sewage outlet is arranged at the bottom of the dirty liquid area.
进一步,所述中空纤维总长度至少为1000mm,数量至少为1.5万根,装入所述超微滤膜过滤器的过滤区后,用密封胶在距离中空纤维开口端20mm处与超微滤膜过滤器固定,且密封胶将超微滤膜过滤器内部分割成为净液区和过滤区。 Further, the total length of the hollow fiber is at least 1000 mm, and the number is at least 15,000. After being loaded into the filtration area of the ultra-microfiltration membrane filter, sealant is used to connect the ultra-microfiltration membrane at a distance of 20 mm from the opening end of the hollow fiber. The filter is fixed, and the sealant divides the inside of the ultra-microfiltration membrane filter into a clean liquid area and a filter area.
通过超微过滤后的酱油或醋清澈透明,长久放置也不会出现沉淀,并且通过循环过滤最大限度地降低了过滤过程中的产品损耗,即在过滤环节产品损耗不到1%。 The soy sauce or vinegar after ultra-micro filtration is clear and transparent, and there will be no precipitation after long-term storage, and the product loss in the filtration process is minimized through circulating filtration, that is, the product loss in the filtration process is less than 1%.
附图说明 Description of drawings
图1为实施例中本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model in the embodiment.
具体实施方式 Detailed ways
下面结合附图对本实用新型的具体实施方式进行说明。 The specific embodiment of the present utility model is described below in conjunction with accompanying drawing.
如图1所示,一种用于酱油、醋的超滤设备包括:前级的活性焦吸附器10和二级的超微滤膜过滤器20; As shown in Figure 1, a kind of ultrafiltration equipment that is used for soy sauce, vinegar comprises: the active coke adsorber 10 of preceding stage and the ultramicrofiltration membrane filter 20 of secondary stage;
超微滤膜过滤器20的内部自下而上分为净液区27和过滤区26,过滤区26内的过滤材料为若干根n型结构中空纤维22。过滤区26设有进液口21和循环出口24,净液区27设有净水出口23。活性焦吸附器10的清液出口16通过连接管与超微滤膜过滤器20的进液口21相连通。 The inside of the ultra-microfiltration membrane filter 20 is divided into a clean liquid area 27 and a filtering area 26 from bottom to top, and the filtering material in the filtering area 26 is several hollow fibers 22 with n-type structure. The filter zone 26 is provided with a liquid inlet 21 and a circulation outlet 24 , and the clean liquid zone 27 is provided with a clean water outlet 23 . The clear liquid outlet 16 of the activated coke adsorber 10 communicates with the liquid inlet 21 of the ultra-microfiltration membrane filter 20 through a connecting pipe.
n型结构下部的两个开口端均用于向外导出酱油或醋的纯净液,纯净液经净液出口23导出;未被滤出的酱油或醋经循环出口24及管路返回到进液口21。循环出口24处依次设置有压力表31和压力控制阀32;进液口21处设置有液体输送泵33,未被滤出的酱油或醋经液体输送泵33返回到超微滤膜过滤器20内进行循环过滤。中空纤维22的材料为聚砜,其外径为400±20μm,内径为250±20μm;所述中空纤维的超微滤膜微孔孔径为0.07-0.08μm。中空纤维总长度至少为1000mm,数量至少为1.5万根,装入超微滤膜过滤器的过滤区26后,用密封胶在距离中空纤维开口端20mm处与超微滤膜过滤器固定,且密封胶将超微滤膜过滤器内部分割成为净液区27和过滤区26。 The two open ends of the lower part of the n-type structure are used to lead out the pure liquid of soy sauce or vinegar, and the pure liquid is exported through the clean liquid outlet 23; the unfiltered soy sauce or vinegar is returned to the liquid inlet through the circulation outlet 24 and the pipeline Mouth 21. A pressure gauge 31 and a pressure control valve 32 are arranged in turn at the circulation outlet 24; a liquid delivery pump 33 is arranged at the liquid inlet 21, and the unfiltered soy sauce or vinegar returns to the ultra-microfiltration membrane filter 20 through the liquid delivery pump 33 In-cycle filtration. The hollow fiber 22 is made of polysulfone with an outer diameter of 400±20 μm and an inner diameter of 250±20 μm; the pore diameter of the ultra-microfiltration membrane of the hollow fiber is 0.07-0.08 μm. The total length of the hollow fiber is at least 1000 mm, and the number is at least 15,000. After being loaded into the filter area 26 of the ultra-microfiltration membrane filter, sealant is used to fix the ultra-microfiltration membrane filter at a distance of 20 mm from the opening end of the hollow fiber, and The sealant divides the inside of the ultra-microfiltration membrane filter into a clean liquid area 27 and a filtering area 26 .
活性焦吸附器10内自下而上设置有污液区12、吸附区13和清液区14,吸附区13内的吸附材料为颗粒度为ф10-15mm活性焦15,活性焦厚度不小于700mm。污液区与吸附区中间设置有下隔膜,清液区与吸附区中间设置有上隔膜。 The activated coke adsorber 10 is equipped with a dirty liquid area 12, an adsorption area 13 and a clear liquid area 14 from bottom to top. The adsorption material in the adsorption area 13 is active coke 15 with a particle size of ф10-15mm, and the thickness of the active coke is not less than 700mm . A lower diaphragm is arranged between the dirty liquid area and the adsorption area, and an upper diaphragm is arranged between the clear liquid area and the adsorption area.
活性焦吸附器10包括原浆进口11、排污口19和清液出口16,待净化处理的原浆或原液通过原浆进口11进入污液区12,原浆在压力或前级储水池的静压下,或水泵压力下,自下而上逆渗透通过吸附区13进入清液区14,原浆经吸附处理后变成清液,清液经清液出口流出,污液区内的污水或杂质可通过排污口19排出。 The activated coke adsorber 10 includes a raw pulp inlet 11, a sewage outlet 19 and a clear liquid outlet 16. The raw pulp or raw liquid to be purified enters the sewage area 12 through the raw pulp inlet 11. Press down, or under the pressure of the water pump, reverse osmosis enters the clear liquid area 14 through the adsorption area 13 from bottom to top, and the raw slurry becomes clear liquid after adsorption treatment, and the clear liquid flows out through the clear liquid outlet, and the sewage in the dirty liquid area or Impurities can be discharged through the sewage outlet 19.
通过压力控制阀32调整超微滤膜过滤器内的压力,压力表31随时监控该压力值,未被过滤的酱油或醋通过液体输送泵又返还到超微滤膜过滤器内进行循环过滤。最后未被过滤的液体或杂质通过排水口29排出。或者在循环出口24处设置排水分路29a,通过设置开启阀门,污液可则直接从排出分路29a排出。 The pressure in the ultra-microfiltration membrane filter is adjusted by the pressure control valve 32, and the pressure gauge 31 monitors the pressure value at any time, and the unfiltered soy sauce or vinegar is returned to the ultra-microfiltration membrane filter by the liquid delivery pump for circulating filtration. Finally, the unfiltered liquid or impurities are discharged through the drain port 29 . Alternatively, a drainage shunt 29a is provided at the circulation outlet 24, and the dirty liquid can be directly discharged from the discharge shunt 29a by setting an opening valve.
以上结合附图仅描述了本申请的几个优选实施例,但本申请不限于此,凡是本领域普通技术人员在不脱离本申请的精神下,做出的任何改进和/或变形,均属于本申请的保护范围。 The above only describes several preferred embodiments of the present application in conjunction with the accompanying drawings, but the present application is not limited thereto, any improvement and/or deformation made by those skilled in the art without departing from the spirit of the present application shall belong to protection scope of this application.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420695514.9U CN204275819U (en) | 2014-11-19 | 2014-11-19 | A kind of ultrafiltration apparatus for soy sauce, vinegar |
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| CN201420695514.9U CN204275819U (en) | 2014-11-19 | 2014-11-19 | A kind of ultrafiltration apparatus for soy sauce, vinegar |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105273974A (en) * | 2015-10-31 | 2016-01-27 | 庞巧兰 | Fruit vinegar filter system |
| CN105768035A (en) * | 2016-03-17 | 2016-07-20 | 华东理工大学 | Membrane clarification and filtration method for soy sauce |
-
2014
- 2014-11-19 CN CN201420695514.9U patent/CN204275819U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105273974A (en) * | 2015-10-31 | 2016-01-27 | 庞巧兰 | Fruit vinegar filter system |
| CN105273974B (en) * | 2015-10-31 | 2018-08-10 | 庞巧兰 | A kind of fruit vinegar filtration system |
| CN105768035A (en) * | 2016-03-17 | 2016-07-20 | 华东理工大学 | Membrane clarification and filtration method for soy sauce |
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