CN201848116U - Novel volatile component condensation and reclamation device - Google Patents
Novel volatile component condensation and reclamation device Download PDFInfo
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- CN201848116U CN201848116U CN2010206041661U CN201020604166U CN201848116U CN 201848116 U CN201848116 U CN 201848116U CN 2010206041661 U CN2010206041661 U CN 2010206041661U CN 201020604166 U CN201020604166 U CN 201020604166U CN 201848116 U CN201848116 U CN 201848116U
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- 238000009833 condensation Methods 0.000 title claims abstract description 37
- 230000005494 condensation Effects 0.000 title claims abstract description 37
- 239000010410 layer Substances 0.000 claims abstract description 22
- 239000011229 interlayer Substances 0.000 claims abstract description 21
- 238000011084 recovery Methods 0.000 claims abstract description 18
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 238000004064 recycling Methods 0.000 abstract description 4
- 238000009835 boiling Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
一种新型易挥发组分冷凝回收装置,包括冷凝罐、循环泵及液泵,所述冷凝罐由容器体、双层盘管组成,其体身外侧设有第二密闭腔的夹层套,双层盘管设于容器体内且盘管进口、盘管出口由容器体的侧壁伸出体外,盘管进口与夹层套出口连接,液泵的输出端与夹层套进口连接、输入端与盘管出口连接,循环泵的输入端与罐体出口连接、输出端与罐体进口连接。本实用新型由冷凝罐内的双层盘管构成内层冷凝,由夹层套构成外层冷凝,循环泵用于保证易挥发组分在反应体系中实现无压差冷凝回收,从而实现对反应体系内的所有易挥发组分最大限度的冷凝回收。具有结构简单、回收产率高、回收成本低的特点。
A new type of condensation recovery device for volatile components, including a condensation tank, a circulation pump and a liquid pump. The condensation tank is composed of a container body and a double-layer coil. The layer coil is set in the container body and the coil inlet and coil outlet protrude from the side wall of the container body, the coil inlet is connected to the outlet of the interlayer sleeve, the output end of the liquid pump is connected to the inlet of the interlayer sleeve, and the input end is connected to the coil The outlet is connected, the input end of the circulation pump is connected with the tank body outlet, and the output end is connected with the tank body inlet. The utility model is composed of a double-layer coil in the condensation tank to form the inner layer of condensation, and an interlayer sleeve to form the outer layer of condensation. The circulation pump is used to ensure that the volatile components can be condensed and recovered without pressure difference in the reaction system, so as to realize the recovery of the reaction system. Maximum condensate recovery of all volatile components within. It has the characteristics of simple structure, high recycling yield and low recycling cost.
Description
技术领域technical field
本实用新型涉及光化学技术领域,适用于在大体积密闭体系中对The utility model relates to the field of photochemical technology, and is suitable for treating
低沸点组分的冷凝回收,尤其是一种易挥发组分的冷凝回收装置。Condensation recovery of low boiling point components, especially a condensation recovery device for volatile components.
背景技术Background technique
现有技术对易挥发组分的冷凝回收所使用的冷凝管一般为球形或蛇形冷凝管,这种冷凝管对有机化合物中易挥发组分的冷凝效果不佳,尤其针对低沸点的易挥发组分,在冷凝过程中,即使通入乙醇、丙酮等低温冷凝回流液体效果也不理想,造成回收产率低、回收成本高的缺陷。The condensing tubes used in the prior art for the condensation and recovery of volatile components are generally spherical or serpentine condensing tubes, which are not effective in condensing volatile components in organic compounds, especially for volatile components with low boiling points. Components, in the condensation process, even if ethanol, acetone and other low-temperature condensation reflux liquids are passed in, the effect is not ideal, resulting in the defects of low recovery yield and high recovery cost.
实用新型内容Utility model content
本实用新型的目的是针对现有技术的不足而提供的一种易挥发The purpose of this utility model is to provide a kind of volatile
组分的冷凝回收装置,具有结构简单、回收产率高、回收成本低的特点。The component condensation recovery device has the characteristics of simple structure, high recovery yield and low recovery cost.
实现本实用新型目的的具体技术方案是:The concrete technical scheme that realizes the utility model purpose is:
一种新型易挥发组分的冷凝回收装置,其特点包括冷凝罐、循环泵及液泵,所述冷凝罐由容器体、双层盘管组成,容器体的体内为第一密闭腔、其顶部设有罐体进口、底部设有生成物出口,其体身外侧设有第二密闭腔的夹层套、夹层套上设有夹层套进口、夹层套出口,容器体内沿内壁设有开口的环状挡板、环状挡板与容器体内壁间构成开放环腔,开放环腔内设有罐体出口,双层盘管由空心管经内外两圈缠绕成螺旋柱状、其上设有盘管进口、盘管出口,双层盘管设于容器体内且盘管进口、盘管出口由容器体的侧壁伸出体外,盘管进口与夹层套出口连接,液泵的输出端与夹层套进口连接、输入端与盘管出口连接,循环泵的输入端与罐体出口连接、输出端与罐体进口连接;所述的循环泵由一组或多组风扇串联组成;所述的容器体的生成物出口上设有第一活塞;所述的循环泵的输入端上设有第二活塞。A new type of condensation recovery device for volatile components, which features a condensation tank, a circulation pump and a liquid pump. The condensation tank is composed of a container body and a double-layer coil. There is a tank body inlet, a product outlet at the bottom, a sandwich sleeve with a second airtight cavity on the outside of the body, an interlayer sleeve inlet and a sandwich sleeve outlet on the interlayer sleeve, and an annular ring with an opening along the inner wall of the container. The baffle, the ring-shaped baffle and the inner wall of the container form an open ring cavity, and the tank body outlet is arranged in the open ring cavity, and the double-layer coil is wound into a spiral column by a hollow tube through two circles inside and outside, and a coil inlet is arranged on it. , coil outlet, the double-layer coil is set in the container body and the coil inlet and coil outlet protrude from the side wall of the container body, the coil inlet is connected to the outlet of the interlayer sleeve, and the output end of the liquid pump is connected to the inlet of the interlayer sleeve , the input end is connected to the coil outlet, the input end of the circulation pump is connected to the tank body outlet, and the output end is connected to the tank body inlet; the circulation pump is composed of one or more sets of fans connected in series; the formation of the container body A first piston is provided on the material outlet; a second piston is provided on the input end of the circulation pump.
本实用新型具有结构简单、回收产率高、回收成本低的特点。The utility model has the characteristics of simple structure, high recycling yield and low recycling cost.
附图说明Description of drawings
图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
具体实施方式Detailed ways
参阅图1,本实用新型包括冷凝罐1、循环泵2及液泵5,所述冷凝罐1由容器体3、双层盘管4组成,容器体3的体内为第一密闭腔、其顶部设有罐体进口35、底部设有生成物出口37,其体身外侧设有第二密闭腔的夹层套31、夹层套31上设有夹层套进口32、夹层套出口33,容器体3内沿内壁设有开口的环状挡板34、环状挡板34与容器体3内壁间构成开放环腔39,开放环腔39内设有罐体出口36,双层盘管4由空心管经内外两圈缠绕成螺旋柱状、其上设有盘管进口41、盘管出口42,双层盘管4设于容器体3内且盘管进口41、盘管出口42由容器体3的侧壁伸出体外,盘管进口41与夹层套出口33连接,液泵5的输出端与夹层套进口32连接、输入端与盘管出口42连接,循环泵2的输入端与罐体出口36连接、输出端与罐体进口35连接;所述的循环泵2由一组或多组风扇22串联组成;所述的容器体3的生成物出口37上设有第一活塞38;所述的循环泵2的输入端上设有第二活塞21。Referring to Fig. 1, the utility model comprises
本实用新型是这样使用的:The utility model uses like this:
参阅图1,易挥发组分由冷凝罐1的罐体进口35进入容器体3内,在双层盘管4的冷凝作用下,在容器体3内完成内层初冷凝,初冷凝后,易挥发组分越过环状挡板34进入开放环腔39,在夹层套31的冷凝作用下,在容器体3内进一步完成外层冷凝,内外层冷凝完成后,冷凝下来的易挥发组分经第一活塞38由生成物出口37回收,未冷凝下来的易挥发组分经罐体出口36、第二活塞21进入循环泵2,通过三组风扇22经罐体进口35返回到容器体3内重新冷凝,通过循环泵2和冷凝罐1的多次循环把反应体系内的所有易挥发组分最大限度的冷凝回收。Referring to Fig. 1, the volatile components enter the container body 3 from the
本实用新型的冷凝液循环过程如下,冷凝液由液泵5的输出端及夹层套进口32进入夹层套31、再由夹层套出口33经盘管进口41进入双层盘管4循环后由盘管出口42补充回到液泵5。The condensate circulation process of the present utility model is as follows, the condensate enters the
本实用新型循环泵2内所用的风扇为四氟耐酸碱风扇。The fan used in the circulation pump 2 of the utility model is a tetrafluoroacid and alkali resistant fan.
本实用新型由冷凝罐1内的双层盘管4构成内层冷凝,通过双层盘管4的冷凝作用对易挥发组分冷凝回收,由夹层套31构成外层冷凝,通过夹层套31对易挥发组分进一步冷凝外,还用于防止低沸点组分的进一步挥发,循环泵2用于保证易挥发组分在密闭负压的反应体系中实现无压差冷凝回收,从而实现对反应体系内的所有易挥发组分最大限度的冷凝回收。The utility model is composed of the double-layer coil 4 in the
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206041661U CN201848116U (en) | 2010-11-12 | 2010-11-12 | Novel volatile component condensation and reclamation device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206041661U CN201848116U (en) | 2010-11-12 | 2010-11-12 | Novel volatile component condensation and reclamation device |
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| CN201848116U true CN201848116U (en) | 2011-06-01 |
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| CN2010206041661U Expired - Fee Related CN201848116U (en) | 2010-11-12 | 2010-11-12 | Novel volatile component condensation and reclamation device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111624059A (en) * | 2020-06-19 | 2020-09-04 | 云南中烟工业有限责任公司 | A flue gas capture device with a serpentine flue gas circulation pipe |
| CN111624058A (en) * | 2020-06-19 | 2020-09-04 | 云南中烟工业有限责任公司 | A cigarette smoke capture device with adjustable length of intake pipe |
-
2010
- 2010-11-12 CN CN2010206041661U patent/CN201848116U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111624059A (en) * | 2020-06-19 | 2020-09-04 | 云南中烟工业有限责任公司 | A flue gas capture device with a serpentine flue gas circulation pipe |
| CN111624058A (en) * | 2020-06-19 | 2020-09-04 | 云南中烟工业有限责任公司 | A cigarette smoke capture device with adjustable length of intake pipe |
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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: 20110601 Termination date: 20161112 |
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| CF01 | Termination of patent right due to non-payment of annual fee |
