CN204455049U - Soap fat fat acid distillation system - Google Patents
Soap fat fat acid distillation system Download PDFInfo
- Publication number
- CN204455049U CN204455049U CN201520097670.XU CN201520097670U CN204455049U CN 204455049 U CN204455049 U CN 204455049U CN 201520097670 U CN201520097670 U CN 201520097670U CN 204455049 U CN204455049 U CN 204455049U
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- Prior art keywords
- fatty acid
- lipid acid
- fat
- acid distillation
- residue
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides a kind of soap fat fat acid distillation system, comprise lipid acid degasser, lipid acid well heater, fatty acid distillation tower, second column, residue water cooler and residue tank, the outlet of described lipid acid degasser lower end is connected with lipid acid well heater refrigerant inlet, described lipid acid well heater refrigerant exit is connected with the feed(raw material)inlet being positioned at fatty acid distillation tower lower end, described fatty acid distillation tower lower end solid discharge is connected with second column feeding mouth, described second column lower end solid discharge is connected with residue water cooler entrance, described residue cooler outlet is connected with residue tank entrance.The utility model is simple and reasonable for structure, compact, optimizes fatty acid distillation program compared with prior art; The utility model, by arranging after-fractionating tower, improves the fatty acid distillation rate of recovery, substantially increases productive rate, increases enterprise income.
Description
Technical field
The utility model relates to soapmaking technology, particularly relates to a kind of soap fat fat acid distillation system.
Background technology
The ultimate principle of fatty acid distillation is different according to lipid acid and mixtures of impurities boiling point, controls certain distillation temperature, by lower-boiling impurity and high-boiling-point impurity and fatty acid separation, thus can reach refining object.The distillation of natural acid, can adopt the device of intermittent type and continous way to carry out, but no matter adopt which kind of form, first must consider the characteristic that lipid acid is the most basic, as boiling point, fusing point etc.
The factor affecting distilled fatty acid quality and yield is a lot, except distil process, distillation plant is the important factor affecting distilling effect, in order to obtain high-quality distilled fatty acid product, the distil process of modern lipid acid needs to pay attention to Railway Project below: the vapour lock of equipment is little, and efficiency wants high; Equipment leakage is few, and vacuum system is efficient, economical.
Utility model content
The purpose of this utility model is, low for above-mentioned existing lipid acid rectifying installation efficiency, and the problem of poor product quality proposes a kind of soap fat fat acid distillation system, and this system is simple, the distillation realizing lipid acid that can be efficient, economic.
For achieving the above object, the technical solution adopted in the utility model is: a kind of soap fat fat acid distillation system, comprise lipid acid degasser, lipid acid well heater, fatty acid distillation tower, second column, residue water cooler and residue tank, the outlet of described lipid acid degasser lower end is connected with lipid acid well heater refrigerant inlet, described lipid acid well heater refrigerant exit is connected with the feed(raw material)inlet being positioned at fatty acid distillation tower lower end, described fatty acid distillation tower lower end solid discharge is connected with second column feeding mouth, described second column lower end solid discharge is connected with residue water cooler entrance, described residue cooler outlet is connected with residue tank entrance.
Further, described lipid acid well heater is hotline heater.
Further, lipid acid degasser feed(raw material)inlet is provided with raw material strainer.
Further, interchanger is provided with between described raw material strainer and lipid acid degasser feed(raw material)inlet.
Further, described fatty acid distillation tower side wall is provided with cycle stock outlet and cycle stock entrance, described fatty acid distillation tower is outside equipped with and loops back chute, described in loop back entrance and the cycle stock outlet at chute top, the outlet of described pump around circuit trench bottom is communicated with cycle stock entrance.
Further, the heating agent of described fatty acid distillation tower is thermal oil.
The principle of work of described soap fat fat acid distillation system is as follows: the degassed → intermittent feeding that intermittently dewaters → steam lipid acid → releasing residue, specifically comprise the following steps: described raw material enters through lipid acid degasser feed(raw material)inlet, complete degassed raw material to heat in lipid acid well heater, enter described fatty acid distillation tower to distill, the light constituent of described fatty acid distillation tower upper end goes to workshop for subsequent use, the residue that described fatty acid distillation tower lower end solid discharge flows out is through the second distillation of second column, ensure the recovery completely of product, the final residue obtained through second distillation is discharged through second column lower end solid discharge, enter after cooling is thought highly of in residue cooling and be collected in residue tank.
A kind of soap fat fat of the utility model acid distillation system architecture is simple, reasonable, compact, optimizes fatty acid distillation program compared with prior art; The utility model, by arranging after-fractionating tower, improves the fatty acid distillation rate of recovery, substantially increases productive rate, increases enterprise income.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model soap fat fat acid distillation system.
Wherein:
1-lipid acid degasser; 2-lipid acid well heater; 3-fatty acid distillation tower; 4-second column; 5-residue water cooler; 6-residue tank; 7-raw material strainer; 8-interchanger.
Embodiment
Below in conjunction with embodiment, the utility model is further illustrated:
Present embodiment discloses a kind of soap fat fat acid distillation system, as shown in Figure 1: comprise lipid acid degasser 1, lipid acid well heater 2, fatty acid distillation tower 3, second column 4, residue water cooler 5 and residue tank 6, described lipid acid well heater 2 is hotline heater, and the heating agent of described fatty acid distillation tower 3 is thermal oil.
The outlet of described lipid acid degasser 1 lower end is connected with lipid acid well heater 2 refrigerant inlet, described lipid acid well heater 2 refrigerant exit is connected with the feed(raw material)inlet being positioned at fatty acid distillation tower 3 lower end, described fatty acid distillation tower 3 lower end solid discharge is connected with second column 4 feeding mouth, described second column 4 lower end solid discharge is connected with residue water cooler 5 entrance, and described residue water cooler 5 outlet is connected with residue tank 6 entrance.
Lipid acid degasser 1 feed(raw material)inlet is provided with raw material strainer 7.Interchanger 8 is provided with between described raw material strainer 7 and lipid acid degasser 1 feed(raw material)inlet.
The principle of work of described soap fat fat acid distillation system is as follows: the degassed → intermittent feeding that intermittently dewaters → steam lipid acid → releasing residue.Specifically comprise the following steps: described raw material enters through lipid acid degasser 1 feed(raw material)inlet, complete degassed raw material to heat in lipid acid well heater 2, enter described fatty acid distillation tower 3 to distill, the light constituent (product) of described fatty acid distillation tower 3 upper end goes to workshop for subsequent use, the residue that described fatty acid distillation tower 3 lower end solid discharge flows out is through the second distillation of second column 4, ensure the recovery completely of product, the final residue obtained through second distillation is discharged through second column 4 lower end solid discharge, enter after residue water cooler 5 heavily cools and be collected in residue tank 6.
Embodiment 2
Present embodiment discloses a kind of fatty acid for soap Distallation systm substantially the same manner as Example 1, unlike described fatty acid distillation tower side wall being provided with cycle stock outlet and cycle stock entrance, described fatty acid distillation tower is outside equipped with and loops back chute, described entrance and the cycle stock outlet looping back chute top, the outlet of described pump around circuit trench bottom is communicated with cycle stock entrance.
Last it is noted that above each embodiment is only in order to illustrate the technical solution of the utility model, be not intended to limit; Although be described in detail the utility model with reference to foregoing embodiments, those of ordinary skill in the art is to be understood that: it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein some or all of technical characteristic; And these amendments or replacement, do not make the essence of appropriate technical solution depart from the scope of each embodiment technical scheme of the utility model.
Claims (5)
1. a soap fat fat acid distillation system, it is characterized in that, comprise lipid acid degasser, lipid acid well heater, fatty acid distillation tower, second column, residue water cooler and residue tank, the outlet of described lipid acid degasser lower end is connected with lipid acid well heater refrigerant inlet, described lipid acid well heater refrigerant exit is connected with the feed(raw material)inlet being positioned at fatty acid distillation tower lower end, described fatty acid distillation tower lower end solid discharge is connected with second column feeding mouth, described second column lower end solid discharge is connected with residue water cooler entrance, described residue cooler outlet is connected with residue tank entrance.
2. soap fat fat acid distillation system according to claim 1, it is characterized in that, described lipid acid well heater is hotline heater.
3. soap fat fat acid distillation system according to claim 1, it is characterized in that, described lipid acid degasser feed(raw material)inlet is provided with raw material strainer.
4. soap fat fat acid distillation system according to claim 3, is characterized in that, be provided with interchanger between described raw material strainer and lipid acid degasser feed(raw material)inlet.
5. soap fat fat acid distillation system according to claim 1, it is characterized in that, described fatty acid distillation tower side wall is provided with cycle stock outlet and cycle stock entrance, described fatty acid distillation tower is outside equipped with and loops back chute, described entrance and the cycle stock outlet looping back chute top, the outlet of described pump around circuit trench bottom is communicated with cycle stock entrance.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520097670.XU CN204455049U (en) | 2015-02-11 | 2015-02-11 | Soap fat fat acid distillation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520097670.XU CN204455049U (en) | 2015-02-11 | 2015-02-11 | Soap fat fat acid distillation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204455049U true CN204455049U (en) | 2015-07-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520097670.XU Expired - Fee Related CN204455049U (en) | 2015-02-11 | 2015-02-11 | Soap fat fat acid distillation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204455049U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112500933A (en) * | 2020-11-20 | 2021-03-16 | 汕头市天汇健生物技术有限公司 | Process for purification of crude fatty acids |
-
2015
- 2015-02-11 CN CN201520097670.XU patent/CN204455049U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112500933A (en) * | 2020-11-20 | 2021-03-16 | 汕头市天汇健生物技术有限公司 | Process for purification of crude fatty acids |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20150708 Termination date: 20200211 |
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| CF01 | Termination of patent right due to non-payment of annual fee |