CN2696709Y - Silk screen foam removing coalescer for separation purifing - Google Patents
Silk screen foam removing coalescer for separation purifing Download PDFInfo
- Publication number
- CN2696709Y CN2696709Y CN 200420040054 CN200420040054U CN2696709Y CN 2696709 Y CN2696709 Y CN 2696709Y CN 200420040054 CN200420040054 CN 200420040054 CN 200420040054 U CN200420040054 U CN 200420040054U CN 2696709 Y CN2696709 Y CN 2696709Y
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- CN
- China
- Prior art keywords
- silk screen
- layer
- separating
- purifing
- coagulator
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- Expired - Fee Related
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Abstract
The utility model provides a silk screen foam removing coagulator for separating and purifing, belonging to the technical field of gas-liquid and liquid-liquid separating and purifying facilities. A silk screen foam removing coagulator for separating and purifing whose pressure is reduced and separating and purifying efficacy is good is provided. The silk screen foam removing coagulator for separating and purifing comprises superimposed silk screen layers and upper and lower barrier plates, a composite layer structure is adopted by the silk screen layers after being improved, the density of the upper layer is larger than the density of the lower layer, and the single layer silk screen in each silk screen layer is misplaced and superimposed. When the utility model works, the gas containing liquid foam or the oil containing foreign matters are firstly rough separated and purified through the silk screen layer of lower density and subtly separated and purified through the silk screen layer of high density. The flow resistance is little on the condition of the integral thickness of the silk screen layers is the same, the pressure is reduced, and the characters that the void rate is large and the contacting of the silk screens and gas is sufficient are provided. The separating and purifying processing quality can be ensured, and the best effect can be obtained by malplacing and superimposing. The consumption of the layer of high density can be reduced and the production cost is reduced. The silk screen foam removing coagulator for separating and purifing is adaptable to be served as the alternating product of the existing silk screen foam removing coagulator to be used.
Description
Technical field
The utility model relates to removes the separating purifying device that the liquid impurities composition is used in the liquid foam and oil product in the gas, belongs to solution-air, liquid-liquid separation and purification facility technical field.
Background technology
Existing isolation of purified screen apparatus is reached by the silk screen that is layering, compositions such as following barrier board, its working mechanism is, silk screen layer is by last, following barrier board is placed in the container body, the oil product etc. that contains the gas of liquid foam or contain impurity such as moisture is during through silk screen layer, wettable at silk screen, under the acting in conjunction of capillarity and surface tension of liquid, dropping liquids such as liquid foam or moisture adhere on the silk screen, and constantly gathering is condensed into bigger drop, when the drop self gravitation surpasses buoyant gas and surface tension of liquid, drop comes off voluntarily, be deposited on container body bottom, thereby realize the isolation of purified of liquid foam and impurity dropping liquid is removed operation.In the existing silk screen separator, multi-layer silk screen is the silk screen of same density, helps to improve the processing quality of isolation of purified when density is higher, but the corresponding resistance that can increase the silk screen layer body produces bigger pressure and falls when gas and liquid are flowed through; It is then just in time opposite to reduce density, falls though can reduce pressure, can have influence on the processing quality of isolation of purified.How solve reasonably that existing pressure in the existing screen apparatus falls and the isolation of purified effect between contradiction, fall with as far as possible little pressure and to obtain high-quality isolation of purified effect, be the key point that improves silk screen separator properties of product.
Summary of the invention
Technical problem to be solved in the utility model provides a kind of silk screen foam-removing and condensation equipment of isolation of purified, to improve the isolation of purified effect, reduces pressure drop, overcomes above-mentioned use defective.
The alleged problem of the utility model realizes with following technical scheme:
A kind of silk screen foam-removing and condensation equipment of isolation of purified has the silk screen layer and the upper and lower barrier board of stack in the formation, its improvement is that described silk screen layer is a lamination layer structure, and each layer density increases progressively from the bottom to top gradually.
The silk screen foam-removing and condensation equipment of above-mentioned isolation of purified, described composite bed are upper and lower two-layer, upper strata silk screen 1 account for composite bed thickness 30～50%, lower floor's silk screen 2 accounts for 70～50% of composite bed thickness.。
The silk screen foam-removing and condensation equipment of above-mentioned isolation of purified, the individual layer silk screen mutual dislocation stack in the described upper and lower layer silk screen.
The silk screen foam-removing and condensation equipment of above-mentioned isolation of purified, described staggered superposition are rotary shifted stack, and the anglec of rotation is 100 °～130 °.
Silk screen layer in the utility model adopts the lamination layer structure design, low-density layer is following, high-density layer is last, contain the gas of liquid foam or impure oil product etc. earlier through purifying than the crude separation of low-density silk screen layer, again through the smart isolation of purified of higher density silk screen layer, under silk screen layer integral thickness the same terms, flow resistance is little, pressure falls little, and it is big to have voidage, the characteristic of silk screen and gas or oil product full contact, thus can guarantee the processing quality of isolation of purified, and handle quality and obtain optimum efficiency by staggered superposition easily; In addition, can reduce production costs because of reduction high-density layer consumptive material, suitable substitute products as existing foam-removing and condensation equipment use.
Description of drawings
Fig. 1 is embodiment 1 structural representation;
Fig. 2 is embodiment 2 structural representations.
The specific embodiment
Consult Fig. 1, embodiment 1 is for being used for the embodiment that isolation of purified gas liquid foam is used.6 is that container body, 3 is last barrier board among the figure, and 4 are following barrier board, and following barrier board 4 is connected with container body 6, and the composite bed silk screen is placed in down on the barrier board 4, and last barrier board 3 is pressed on the composite bed silk screen, and press strip 5 is used to push down barrier board 3.The silk of each layer silk screen is through being 0.2～0.25 millimeter in the upper and lower layer silk screen 1,2, and the density of upper strata silk screen 1 is 60 holes/100 centimeter length, and the density of lower floor's silk screen 2 is 40 holes/100 centimeter length.The gas that contains the liquid foam is entered by the air inlet 7 of container body 6 belows, handles the back through composite bed silk screen isolation of purified and is discharged by the outlet 8 at container body top, and the drop that sticks on the upper and lower silk screen layer is deposited into container body bottom, is discharged by floss hole 9.
Consult Fig. 2, embodiment 2 is used for impurity such as the moisture, alkali lye of isolation of purified oil product.Container body 6 horizontal settings this moment, upper and lower barrier board 3,4 is the positioned vertical state, and the composite bed silk screen is arranged in upper and lower barrier board, and fluid is entered by the import 7 on the right, derived by the outlet 8 on the left side behind isolation of purified, drop is deposited into dehydration bag 10 backs of container body bottom by floss hole 9 dischargings.
Consult accompanying drawing, staggered superposition is adopted in the stack of upper and lower layer silk screen 1,2 silk screens, can adopt rotary shifted stack, certainly, also can adopt laterally or the staggered superposition of directed displacement vertically etc.Adopt when rotary shifted, the anglec of rotation can be 100～130 °, can left and rightly revolve alternately staggered superposition, also can equidirectional rotary shifted successively stack.Among the embodiment 1,2, upper strata silk screen 1 account for whole composite bed thickness 30～50%, lower floor's silk screen 2 accounts for 70～50% of whole composite bed thickness.The thickness of whole composite bed silk screen is decided on treatment media and container body size etc.
Claims (4)
1. the silk screen foam-removing and condensation equipment of an isolation of purified has the silk screen layer and the upper and lower barrier board of stack in the formation, it is characterized in that described silk screen layer is a lamination layer structure, and each layer density increases progressively from the bottom to top gradually.
2. the silk screen foam-removing and condensation equipment of isolation of purified according to claim 1 is characterized in that, described composite bed is upper and lower two-layer, upper strata silk screen 1 account for composite bed thickness 30～50%, lower floor's silk screen 2 accounts for 70～50% of composite bed thickness.。
3. the silk screen foam-removing and condensation equipment of isolation of purified according to claim 1 and 2 is characterized in that, the individual layer silk screen mutual dislocation stack in the described upper and lower layer silk screen.
4. the silk screen foam-removing and condensation equipment of isolation of purified according to claim 3 is characterized in that, described staggered superposition can be rotary shifted stack, and the anglec of rotation is 100 °～130 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420040054 CN2696709Y (en) | 2004-04-15 | 2004-04-15 | Silk screen foam removing coalescer for separation purifing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420040054 CN2696709Y (en) | 2004-04-15 | 2004-04-15 | Silk screen foam removing coalescer for separation purifing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2696709Y true CN2696709Y (en) | 2005-05-04 |
Family
ID=34774134
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200420040054 Expired - Fee Related CN2696709Y (en) | 2004-04-15 | 2004-04-15 | Silk screen foam removing coalescer for separation purifing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2696709Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103864163A (en) * | 2014-03-27 | 2014-06-18 | 广州中国科学院先进技术研究所 | Combined type nonmetal sea water desalination demister |
| CN110548350A (en) * | 2019-10-09 | 2019-12-10 | 浙江强盛压缩机制造有限公司 | low-pressure low-flow-rate efficient gas-liquid separation tank |
-
2004
- 2004-04-15 CN CN 200420040054 patent/CN2696709Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103864163A (en) * | 2014-03-27 | 2014-06-18 | 广州中国科学院先进技术研究所 | Combined type nonmetal sea water desalination demister |
| CN110548350A (en) * | 2019-10-09 | 2019-12-10 | 浙江强盛压缩机制造有限公司 | low-pressure low-flow-rate efficient gas-liquid separation tank |
| CN110548350B (en) * | 2019-10-09 | 2021-07-20 | 浙江强盛压缩机制造有限公司 | Low-pressure low-flow-rate efficient gas-liquid separation tank |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |