CN203487065U - Isooctyl palmitate alcohol-removing device - Google Patents
Isooctyl palmitate alcohol-removing device Download PDFInfo
- Publication number
- CN203487065U CN203487065U CN201320610013.1U CN201320610013U CN203487065U CN 203487065 U CN203487065 U CN 203487065U CN 201320610013 U CN201320610013 U CN 201320610013U CN 203487065 U CN203487065 U CN 203487065U
- Authority
- CN
- China
- Prior art keywords
- tower
- interchanger
- condenser
- pipe
- heat exchanger
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model relates to an isooctyl palmitate alcohol-removing device which comprises a filler tower with a tower cap, a heat exchanger and a condenser, wherein the top of the tower cap of the filler tower is connected with a steam discharge pipe, the steam discharge pipe is connected with a hot fluid inlet of the heat exchanger, a hot fluid outlet of the heat exchanger is connected with the inlet of the condenser, and the outlet of the condenser is connected with an isooctanol receiving tank. The upper part of the filler tower is connected with a feed pipe which is connected with a cold fluid outlet of the heat exchanger, and a cold fluid inlet of the heat exchanger is taken as a material inlet. A steam inlet pipe is connected to the side wall at the bottom of the filler tower, and a tower kettle is connected below the filler tower. The device provided by the utility model has the beneficial effects that the device is simple and convenient to operate and low in energy consumption; residual isooctanol in isooctyl palmitate can be separated, and the separated isooctanol can be used as a raw material for production, so that the energy sources are saved.
Description
Technical field
The utility model relates to a kind of iso-octyl palmitate except alcohol device.
Background technology
Iso-octyl palmitate is mainly used in toiletries, its perviousness is good, tool antiperspirant effect, strong with skin avidity, for the ventilative oil of dryness, being widely used in skin care product and makeup, is good skin emollients, its stable performance, not oxidizable or produce peculiar smell, can make skin soft soft and without greasy feeling, good penetrability, is usually used in all kinds of protective skin cream.In makeup as the good solvent of pigment in the associating agent of extension agent, press-powder formula makeup and color make-up.Be usually used in foundation cream, in the formula such as sunscreen products, eye shadow, lipstick, Mascara.Also can be used as tenderizer, dispersion agent, application in the formulas such as profit hair-cream, body wash.
In the product of traditional mode of production, remain isooctyl alcohol, isooctyl alcohol can make product emit bad smell, the method of removing isooctyl alcohol is now distilled exactly, and the product distilling has the rancidity of one dry grease, has seriously restricted its interpolation in many scopes and has used.
Summary of the invention
For solving above technical deficiency, the utility model provides a kind of iso-octyl palmitate that can remove peculiar smell except alcohol device, has greatly improved the quality of product.
The utility model is realized by following measures:
A kind of iso-octyl palmitate of the present utility model is except alcohol device, comprise packing tower, interchanger and condenser with tower cap, the tower crown portion of described packing tower is connected with steam discharge pipe, described steam discharge pipe connects the hot-fluid import of interchanger, the hot-fluid outlet of interchanger connects the import of condenser, and the outlet of condenser is connected with isooctyl alcohol receiving tank; Described packing tower top is connected with feed-pipe, and described feed-pipe connects the cold fluid outlet of interchanger, and the cold fluid import of interchanger is as material inlet; On the sidewall of packing tower bottom, be connected with steam inlet tube, packing tower below is connected with tower reactor, and described tower reactor and isooctyl alcohol receiving tank bottom are provided with water-and-oil separator.
The mouth of pipe that above-mentioned feed-pipe is positioned at packing tower is connected with sparger.
The beneficial effects of the utility model are: simple to operation, energy consumption is low, isooctyl alcohol residual in iso-octyl palmitate can be separated, and the isooctyl alcohol of separating can be used as raw material for the production of, save the energy.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Wherein: 1 packing tower, 2 steam inlet tubes, 3 tower reactors, 4 isooctyl alcohol receiving tanks, 5 condensers, 6 interchanger, 7 steam discharge pipes, 8 tower caps, 9 feed-pipes, 10 spargers.
Embodiment
As shown in Figure 1, a kind of iso-octyl palmitate of the present utility model is except alcohol device, comprise packing tower 1, interchanger 6 and condenser 5 with tower cap 8, tower cap 8 tops of packing tower 1 are connected with steam discharge pipe 7, steam discharge pipe 7 connects the hot-fluid import of interchanger 6, the hot-fluid outlet of interchanger 6 connects the import of condenser 5, and the outlet of condenser 5 is connected with isooctyl alcohol receiving tank 4.Packing tower 1 top is connected with feed-pipe 9, and feed-pipe 9 connects the cold fluid outlet of interchanger 6, and the cold fluid import of interchanger 6 is as material inlet.On packing tower 1 bottom sidewall, be connected with steam inlet tube 2, packing tower 1 below is connected with tower reactor 3, and tower reactor 3 and isooctyl alcohol receiving tank 4 bottoms are provided with water-and-oil separator.The mouth of pipe that feed-pipe 9 is positioned at packing tower 1 is connected with sparger 10.
Its principle of work is: the iso-octyl palmitate containing isooctyl alcohol enters from the cold fluid import of interchanger 6, then through feed-pipe 9, enters in packing tower 1.Now steam enters packing tower 1 from steam inlet tube 2, steam is taken away the isooctyl alcohol in iso-octyl palmitate in the interior uphill process of packing tower 1, and through steam discharge pipe 7, from the hot-fluid import of interchanger 6, enter interchanger 6 together, because the vapor temperature that contains isooctyl alcohol is higher, therefore as heating agent by the heating of the iso-octyl palmitate containing isooctyl alcohol in interchanger 6, self cooling.The iso-octyl palmitate containing isooctyl alcohol after heating is more easily isolated isooctyl alcohol.The steam that contains isooctyl alcohol after cooling enters into the interior further cooling of condenser 5, is finally condensed into liquid and flow in isooctyl alcohol receiving tank 4.And removed the iso-octyl palmitate after isooctyl alcohol because action of gravity enters in tower reactor 3.Water-and-oil separator is separated with iso-octyl palmitate by the water in tower reactor 3, and water-and-oil separator is separated with isooctyl alcohol by the water in isooctyl alcohol receiving tank 4.The isooctyl alcohol of separating can be used as raw material for the production of.
The above is only the preferred implementation of this patent; it should be pointed out that for those skilled in the art, do not departing under the prerequisite of the art of this patent principle; can also make some improvement and replacement, these improvement and replacement also should be considered as the protection domain of this patent.
Claims (3)
1. an iso-octyl palmitate is except alcohol device, it is characterized in that: comprise packing tower, interchanger and condenser with tower cap, the tower crown portion of described packing tower is connected with steam discharge pipe, described steam discharge pipe connects the hot-fluid import of interchanger, the hot-fluid outlet of interchanger connects the import of condenser, and the outlet of condenser is connected with isooctyl alcohol receiving tank; Described packing tower top is connected with feed-pipe, and described feed-pipe connects the cold fluid outlet of interchanger, and the cold fluid import of interchanger is as material inlet; On the sidewall of packing tower bottom, be connected with steam inlet tube, packing tower below is connected with tower reactor.
2. iso-octyl palmitate, except alcohol device, is characterized in that according to claim 1: described tower reactor and isooctyl alcohol receiving tank bottom are provided with water-and-oil separator.
3. iso-octyl palmitate, except alcohol device, is characterized in that: the mouth of pipe that described feed-pipe is positioned at packing tower is connected with sparger according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320610013.1U CN203487065U (en) | 2013-09-30 | 2013-09-30 | Isooctyl palmitate alcohol-removing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320610013.1U CN203487065U (en) | 2013-09-30 | 2013-09-30 | Isooctyl palmitate alcohol-removing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203487065U true CN203487065U (en) | 2014-03-19 |
Family
ID=50257910
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320610013.1U Expired - Fee Related CN203487065U (en) | 2013-09-30 | 2013-09-30 | Isooctyl palmitate alcohol-removing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203487065U (en) |
-
2013
- 2013-09-30 CN CN201320610013.1U patent/CN203487065U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104606909B (en) | One kind of plant Oleum sesami boiler | |
| CN201610426U (en) | Distilling still used for extracting natural essential oil | |
| CN102776074A (en) | Method for producing fatty acid from plant oil scraps | |
| CN204502440U (en) | One Plants sesame oil boiler | |
| CN202430144U (en) | D-bomeol extraction equipment suitable for field sites | |
| CN206127245U (en) | Distillation edulcoration device of raw oil | |
| CN203487065U (en) | Isooctyl palmitate alcohol-removing device | |
| CN203487066U (en) | Isopropyl myristate deodorizing device | |
| CN204767503U (en) | Stills for chemical industry | |
| CN204601640U (en) | A kind of outer circulation alcohol recovery system | |
| CN114516785B (en) | Method and equipment for processing high-purity anethole by using star anise oil | |
| CN201411451Y (en) | Distiller for wine processing | |
| CN100510041C (en) | Preparation process of high content conjugated unsaturated trienic acid granada seed oil | |
| CN201873660U (en) | High-acidity oil physical refining deacidification tower | |
| CN201426985Y (en) | Novel glycerin distillation device | |
| CN208823967U (en) | A kind of glycerol distillation device | |
| CN208586265U (en) | A kind of eucalyptus oil finished product crystallization treatment device | |
| CN104611135A (en) | Yerba mate essential oil | |
| CN204265469U (en) | A kind of negative pressure ammonia still | |
| CN202122841U (en) | Plant essence extractor | |
| CN207775182U (en) | A kind of orange oil distillation processing concentrator | |
| CN102924231B (en) | For producing the method and apparatus of the triple effect distillation of alcohol | |
| CN202961938U (en) | Efficient extracting device beneficial for extracting volatile active ingredients from plants | |
| CN206014731U (en) | A kind of with except alcohol effect iso-octyl palmitate preparation facilitiess | |
| CN201915077U (en) | Oil and fat refining production device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140319 Termination date: 20170930 |