CN203264434U - Energy-saving type distillation-free circular stirring, filtering and bleaching adsorption device for dry cleaning solvent - Google Patents
Energy-saving type distillation-free circular stirring, filtering and bleaching adsorption device for dry cleaning solvent Download PDFInfo
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- CN203264434U CN203264434U CN 201320282926 CN201320282926U CN203264434U CN 203264434 U CN203264434 U CN 203264434U CN 201320282926 CN201320282926 CN 201320282926 CN 201320282926 U CN201320282926 U CN 201320282926U CN 203264434 U CN203264434 U CN 203264434U
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- separator box
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- 238000003756 stirring Methods 0.000 title claims abstract description 63
- 238000001914 filtration Methods 0.000 title claims abstract description 36
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 15
- 238000005108 dry cleaning Methods 0.000 title abstract description 13
- 238000004061 bleaching Methods 0.000 title abstract description 7
- 239000002904 solvent Substances 0.000 title abstract description 5
- 239000000835 fiber Substances 0.000 claims abstract description 26
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 15
- 239000007921 spray Substances 0.000 claims abstract description 13
- 239000000446 fuel Substances 0.000 claims description 17
- 238000004042 decolorization Methods 0.000 claims description 12
- 238000001704 evaporation Methods 0.000 claims description 12
- 238000002156 mixing Methods 0.000 claims description 8
- 238000005255 carburizing Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 6
- 238000004140 cleaning Methods 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract 7
- 239000012459 cleaning agent Substances 0.000 description 6
- 238000004821 distillation Methods 0.000 description 5
- 238000000746 purification Methods 0.000 description 5
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 229950011008 tetrachloroethylene Drugs 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 230000007096 poisonous effect Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The utility model discloses an energy-saving type distillation-free circular stirring, filtering and bleaching adsorption device for a dry cleaning solvent. The device comprises a primary filter tank, a fine filter tank, a fine separation tank and an oil storage tank, wherein cylinder-shaped filter cores are arranged in the primary filter tank, and the bottoms of the cylinder-shaped filter cores are connected with the fine filter tank through flow guide tubes; filter bags are arranged at the top of the fine filter tank, and openings of the filter bags are communicated with the primary filter tank; a plurality of fiber bundles are arranged at the bottom of the fine filter tank; a plurality of fiber bundles are arranged in the fine separation tank, and the fiber bundles are connected with the oil storage tank; a circular stirring and bleaching separation tank is arranged between the fine filter tank and the fine separation tank; and a plurality of cylinder-shaped filter cores and a stirring spray system are arranged at the upper end in the circular stirring and bleaching separation tank, and a plurality of fiber bundles and a carclazyte active carbon layer are arranged at the bottom in the circular stirring and bleaching separation tank. The device has the advantages that the structure is simple, the use is convenient, the cost is low, the filtering, purifying and blenching processes are quick, the mounting and dismounting processes are convenient, the cleaning is easy, and carclazyte and active carbon in the circular stirring and bleaching separation tank are long in service life and can be repeatedly recycled.
Description
Technical field
The utility model relates to a kind of energy-saving non-evaporating DC naphtha circulation stirring that heats up in a steamer and filters the decolorization adsorption device.
Background technology
Dry-cleaning be with the organic chemistry solvent to clothing wash, a kind of dried mode of washing that advances to do of wipe oil or spot.The main feature of dry-cleaning is exactly to avoid washing the injury that the clothing fabric is caused, and shrink-proof, indeformable, nondiscolouring, color and luster protectiveness are good, be difficult for causing clothing fade, soft, be convenient to press and thorough greasy dirt or the spot on cleaning clothes.
The DC naphtha that uses in the market has tetrachloroethylene dry-cleaning agent (poisonous) and oil dry cleaning agent (environmental protection).Due to cost, DC naphtha adopts the mode that recycles to carry out substantially, and the DC naphtha after repeatedly recycling becomes dirty oil because of impure, needs filtration, purification just can reuse.
For different DC naphthas, different purification styles is arranged: it is to adopt high temperature to add the way of distillation that tetrachloroethylene dry-cleaning agent recycles, the dry cleaner's naphtha heating is become gas reclaims by condensation again, whole process is consuming time, power consumption, oil consumption cost are high, distillation one less important three hours.The residue that contains tetrachloro-ethylene thickness congee impurity after distillation is directly discharged sewer, and water quality and ecological environment are polluted.After distillation, the residue in case must be opened manual cleaning, uses poisonous tetrachloro-ethylene to be exposed in air working environment is polluted, and has a strong impact on staff's health.
The oil dry cleaning agent is famous with environmental protection, but, explosive during recycling all the adopted method of filtering inflammable because of the oil dry cleaning agent, after being filtered, used dry cleaning agent just reuses, the magazine that can not thoroughly remove in solvent reduces the dry cleaner's naphtha wash degree, dry-cleaning of garments is unclean, purify loaded down with trivial detailsly, cost is high.
All there is serious defective in the distil(l) of above-mentioned two kinds of DC naphthas, manufacturing process is complicated, use cost is high, clothes after consuming time, power consumption, dry-cleaning can not really reach clean hygiene, and rise because no-cooling-water can cause temperature in dry washer still box inside, pressure is excessive, and serious also can blast, and has potential safety hazard.The residue that contains DC naphtha thickness congee material after distillation is directly discharged sewer water quality and ecological environment is polluted.
Present DC naphtha purifier is installed complicated, need to carry out the multiple filtration purification and decoloration just achieves the goal, and use the carclazyte and active carbon removing that need after a period of time to carry out to the inefficacy of filter core, but present filter cartridge construction is special, dismounting is inconvenient, can not remove carclazyte and active carbon in filter core, can only integral body discard, cause the problems such as waste, pollution, add that present mistake filter element cleaning is more difficult.
The utility model content
The purpose of this utility model be to provide a kind of simple in structure, easy to use, cost is low, filtration, purification decolouring fast, installation and removal are convenient, easily clean, carclazyte and active carbon long service life in circulation stirring decolouring separator box, the energy-saving non-evaporating DC naphtha circulation stirring that heats up in a steamer of recycled for multiple times filters the decolorization adsorption device.
To achieve these goals, the technical solution of the utility model is: provide the energy-saving non-evaporating DC naphtha circulation stirring that heats up in a steamer to filter the decolouring adsorption device, comprise successively from top to bottom primary filter case, fine filtering case, circulation stirring decolouring separator box, meticulous separator box and fuel reserve tank; Primary filter case top is provided with inlet, is provided with several cylindrical filter cores of crossing side by side in the primary filter case, and the cylindrical filter core bottom crossed is connected with the fine filtering case by mozzle; The fine filtering box top is provided with several filter bags side by side, and the filter bag opening communicates with the primary filter case; Fine filtering case bottom is provided with several fibre bundles side by side; Be provided with several fibre bundles side by side in meticulous separator box, described fibre bundle is connected with fuel reserve tank; Wherein, be provided with circulation stirring decolouring separator box between described fine filtering case and meticulous separator box; In circulation stirring decolouring separator box, the upper end is provided with several cylindrical filter core and stirring spray systems crossed side by side, and circulation stirring decolouring separator box inner bottom part is provided with several fibre bundle and carclazyte active carbon layers side by side; Fibre bundle in circulation stirring decolouring separator box communicates with meticulous separator box.
The stirring shower that described stirring spray system comprises mixing pump, be connected with mixing pump and be located at several spray apertures that stir on shower.
Be provided with the breather line that communicates between described primary filter case, fine filtering case, meticulous separator box, circulation stirring decolouring separator box and fuel reserve tank.
Be connected with circulation stirring cylindrical in separator box of described primary filter case is crossed the filter core bottom and is connected with scavenge pipe, and described scavenge pipe is connected with fuel reserve tank, and scavenge pipe is provided with oil pump and corresponding valve.
Described circulation stirring decolouring separator box is provided with carburizing hole and clear carbon mouth.
Description of drawings
Fig. 1 is the energy-saving non-evaporating structural representation that heats up in a steamer DC naphtha dynamic filtration decolorization adsorption device of the utility model;
In figure: 1, inlet; 2, primary filter case; 3, seal cover; 4, the cylindrical filter core of crossing; 5, valve; 6, valve; 7, scavenge pipe; 8, fine filtering case; 9, stir shower; 10, the circulation stirring decolouring separates pure case; 11, mixing pump; 12, fibre bundle; 13, meticulous separator box; 14, fuel reserve tank; 15, oil pump; 16, fibre bundle; 17, carclazyte active carbon layer; 18, spray apertures; 19, fibre bundle; 20, filter bag; 21, breather line; 22, dismounting mouth; 28, valve; 29, valve.
The specific embodiment
For describe the energy-saving non-evaporating technology contents that heats up in a steamer DC naphtha dynamic filtration decolorization adsorption device of the utility model, structural feature in detail, below in conjunction with embodiment and coordinate accompanying drawing to be described further.
As shown in Figure 1, the energy-saving non-evaporating DC naphtha dynamic filtration decolorization adsorption device that heats up in a steamer of the utility model comprises primary filter case 2, fine filtering case 8, meticulous separator box 13 and fuel reserve tank 14 from top to bottom successively; Primary filter case 2 tops are provided with inlet 1, are provided with several cylindrical filter cores 4 of crossing side by side in primary filter case 2, and the cylindrical filter core top crossed is provided with seal cover 3, and the cylindrical filter core bottom crossed is connected with fine filtering case 8 by mozzle; Fine filtering case 8 tops are provided with several filter bags 20 side by side, and the filter bag opening communicates with primary filter case 2; Fine filtering case 8 bottoms are provided with several fibre bundles 19 side by side; Fibre bundle 18 communicates with circulation stirring decolouring separator box 10; Be provided with several fibre bundles 16 side by side in meticulous separator box 13, fibre bundle 16 communicates with fuel reserve tank 14; Be provided with circulation stirring decolouring separator box 10 between described fine filtering case 8 and meticulous separator box 13; The interior upper end of circulation stirring decolouring separator box 10 is provided with several cylindrical filter core and stirring spray systems crossed side by side, and circulation stirring decolouring separator box inner bottom part is provided with several fibre bundle 12 and carclazyte active carbon layers 17 side by side; Fibre bundle 12 in circulation stirring decolouring separator box communicates with meticulous separator box 13.
The stirring shower 9 that described stirring spray system comprises mixing pump 11, be connected with mixing pump and be located at several spray apertures 18 that stir on shower.Be provided with the breather line 21 that communicates between described primary filter case 2, fine filtering case 8, meticulous separator box 13, circulation stirring decolouring separator box 10 and fuel reserve tank 14.
Be connected with circulation stirring cylindrical in separator box 10 of described primary filter case 2 is crossed the filter core bottom and is connected with scavenge pipe 7, and scavenge pipe 7 is connected with fuel reserve tank 14, and scavenge pipe 7 is provided with oil pump 15 and corresponding valve 5 and valve 6.
Be equipped with dismounting mouthfuls 22 on described primary filter case 2, fine filtering case 8, meticulous separator box 13, circulation stirring decolouring separator box 10 and fuel reserve tank 14, be used for that dismounting is cleaned or the work such as maintenance.Also be provided with carburizing hole and clear carbon mouth on described circulation stirring decolouring separator box.
when needing the filtration, purification DC naphtha, pour DC naphtha into primary filter case 2 by inlet 1, open valve 28 and valve 29, valve-off 5 and valve 6 are opened mixing pump 11 simultaneously, open and stir spray system, DC naphtha flows to the filter core inboard from the cylindrical filter core of each of primary filter case 2 outside screen pack, flow to fine filtering case 8 from mozzle again, the DC naphtha of other parts flows to fine filtering case 8 after the opening process filter bag filtration of filter bag 20 simultaneously, cylindrical filter core excessively and filter bag all filter out a part of impurity in DC naphtha, the filtrate that flows to fine filtering case 8 flows to circulation stirring decolouring separator box 10 by the filtration again of fibre bundle 19 again, carclazyte active carbon layer 17 continuous circulation stirring under the effect of stirring spray system in circulation stirring decolouring this moment separator box 10, decoloured fast after DC naphtha filtrate process circulation stirring decolouring this moment separator box 10, filtrate after decolouring is again filtered by fibre bundle 12 at last and is flowed to meticulous separator box 13, and then arrive fuel reserve tank 14 through fibre bundle 16, last fuel reserve tank obtains clean limpid colourless dry-cleaning liquid.When needs rinsed cylindrical filter core excessively, by Open valve 5 and valve 6, valve-off 28 and valve 29 were opened oil pump 15, and the clean solvent in fuel reserve tank is rinsed the cylindrical filter core of crossing.
Due to carclazyte and the continuous circulation stirring of active carbon layer in the utility model circulation stirring decolouring separator box 10, to realize fast filtrate being carried out adsorption bleaching, decolorization rate is fast, and is effective, the long service life of carclazyte and active carbon.
Above disclosed is only preferred embodiment of the present utility model, certainly can not limit with this interest field of the utility model, and the equivalent variations of therefore doing according to the utility model claim still belongs to the scope that the utility model is contained.
Claims (5)
1. the energy-saving non-evaporating DC naphtha circulation stirring that heats up in a steamer filters the decolorization adsorption device, comprises successively from top to bottom primary filter case, fine filtering case, meticulous separator box and fuel reserve tank; Primary filter case top is provided with inlet, is provided with several cylindrical filter cores of crossing side by side in the primary filter case, and the cylindrical filter core bottom crossed is connected with the fine filtering case by mozzle; The fine filtering box top is provided with several filter bags side by side, and the filter bag opening communicates with the primary filter case; Fine filtering case bottom is provided with several fibre bundles side by side; Be provided with several fibre bundles side by side in meticulous separator box, described fibre bundle is connected with fuel reserve tank; It is characterized in that: be provided with circulation stirring decolouring separator box between described fine filtering case and meticulous separator box; In circulation stirring decolouring separator box, the upper end is provided with several cylindrical filter core and stirring spray systems crossed side by side, and circulation stirring decolouring separator box inner bottom part is provided with several fibre bundle and carclazyte active carbon layers side by side; Fibre bundle in circulation stirring decolouring separator box communicates with meticulous separator box.
2. the energy-saving non-evaporating DC naphtha circulation stirring that heats up in a steamer as claimed in claim 1 filters the decolorization adsorption device, it is characterized in that: the stirring shower that described stirring spray system comprises mixing pump, be connected with mixing pump and be located at several spray apertures on the stirring shower.
3. the energy-saving non-evaporating DC naphtha circulation stirring that heats up in a steamer as claimed in claim 1 filters the decolorization adsorption device, it is characterized in that: be provided with the breather line that communicates between described primary filter case, fine filtering case, meticulous separator box, circulation stirring decolouring separator box and fuel reserve tank.
4. the energy-saving non-evaporating DC naphtha circulation stirring that heats up in a steamer as claimed in claim 1 filters the decolorization adsorption device, it is characterized in that: be connected with circulation stirring cylindrical in separator box of described primary filter case is crossed the filter core bottom and is connected with scavenge pipe, described scavenge pipe is connected with fuel reserve tank, and scavenge pipe is provided with oil pump and corresponding valve.
5. the energy-saving non-evaporating DC naphtha circulation stirring that heats up in a steamer as claimed in claim 1 filters the decolorization adsorption device, it is characterized in that: described circulation stirring decolouring separator box is provided with carburizing hole and clear carbon mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320282926 CN203264434U (en) | 2013-05-22 | 2013-05-22 | Energy-saving type distillation-free circular stirring, filtering and bleaching adsorption device for dry cleaning solvent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320282926 CN203264434U (en) | 2013-05-22 | 2013-05-22 | Energy-saving type distillation-free circular stirring, filtering and bleaching adsorption device for dry cleaning solvent |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203264434U true CN203264434U (en) | 2013-11-06 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320282926 Expired - Fee Related CN203264434U (en) | 2013-05-22 | 2013-05-22 | Energy-saving type distillation-free circular stirring, filtering and bleaching adsorption device for dry cleaning solvent |
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| Country | Link |
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| CN (1) | CN203264434U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108193448A (en) * | 2017-12-28 | 2018-06-22 | 山东龙力电器有限公司 | A kind of dry cleaner convenient for application |
-
2013
- 2013-05-22 CN CN 201320282926 patent/CN203264434U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108193448A (en) * | 2017-12-28 | 2018-06-22 | 山东龙力电器有限公司 | A kind of dry cleaner convenient for application |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Free format text: FORMER OWNER: HU-WANG YIBING Effective date: 20150205 Owner name: HAIKOU HUIMEIJIE ENVIRONMENTAL TECHNOLOGY CO., LTD Free format text: FORMER OWNER: LI HONGXUE Effective date: 20150205 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20150205 Address after: 10, B8 building, 570000 floor, Jialing International Building, China World Trade Center Road, Haikou, Hainan Patentee after: Haikou Hui Jie Jie environmental protection technology Co., Ltd. Address before: 570000 Hainan city of Haikou province Qiongzhou Avenue South Road No. 1 ande Park District 5 single room 602 yuan Patentee before: Li Hongxue Patentee before: Hu-Wang Yibing |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131106 Termination date: 20180522 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |