CN204455052U - Soapmaking high pressure grease hydrolysis system - Google Patents
Soapmaking high pressure grease hydrolysis system Download PDFInfo
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- CN204455052U CN204455052U CN201520097673.3U CN201520097673U CN204455052U CN 204455052 U CN204455052 U CN 204455052U CN 201520097673 U CN201520097673 U CN 201520097673U CN 204455052 U CN204455052 U CN 204455052U
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- grease
- hydrolysis
- lipid acid
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- high pressure
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Abstract
The utility model provides a kind of soapmaking high pressure grease hydrolysis system, comprises grease degasser, hydrolysis tower, lipid acid water cooler, lipid acid subsider, sugar water flash tank, sugar water subsider; Described grease degasser discharge port is communicated with hydrolysis tower opening for feed, described hydrolysis tower lower end products export is communicated with the feeding mouth of sugar water flash tank upper end, the discharge port of described sugar water flash tank lower end is communicated with sugar water subsider, described hydrolysis tower upper end discharge port is communicated with lipid acid water cooler upper end, described lipid acid water cooler lower end discharge port is communicated with lipid acid subsider, described hydrolysis tower sidewall upper is provided with more than 3 higher pressure steam inlet, described hydrolysis tower sidewall is also provided with condensation-water drain, for collecting the condensed water of condensation of high pressure steam.This system is simple, reasonable, compact, can realize the hydrolysis of grease efficiently, fast.
Description
Technical field
The utility model relates to soapmaking technology, particularly relates to a kind of soapmaking high pressure grease hydrolysis system.
Background technology
In current China soap industry, the manufacture route of the hydrolysis of many employings paper using, fatty acid distillation and neutralization, the principal feature of high-quality hydrolysis soap preparing process is that hydrolysed fat acid can obtain oil fatty acid through distillation, and the low fat grease being applicable to soapmaking as long as any just can become through hydrolysis-distillation the glyceride stock producing perfumed soap.Existing fat hydrolysis plant efficiency is low, poor controllability, cannot meet the development need of soapmaking industry.
Utility model content
The purpose of this utility model is, low for above-mentioned existing fat hydrolysis system efficiency, the problem of hydrolysis rate poor controllability, and propose a kind of soapmaking high pressure grease hydrolysis system, this system is simple, reasonable, compact, can realize the hydrolysis of grease efficiently, fast.
For achieving the above object, the technical solution adopted in the utility model is: a kind of soapmaking high pressure grease hydrolysis system, comprises grease degasser, hydrolysis tower, lipid acid water cooler, lipid acid subsider, sugar water flash tank, sugar water subsider; Described grease degasser discharge port is communicated with hydrolysis tower opening for feed, described hydrolysis tower lower end products export is communicated with the feeding mouth of sugar water flash tank upper end, the discharge port of described sugar water flash tank lower end is communicated with sugar water subsider, described hydrolysis tower upper end discharge port is communicated with lipid acid water cooler upper end, described lipid acid water cooler lower end discharge port is communicated with lipid acid subsider, described hydrolysis tower sidewall upper is provided with more than 3 higher pressure steam inlet, described hydrolysis tower sidewall is also provided with condensation-water drain, for collecting the condensed water of condensation of high pressure steam.
Further, described grease degasser opening for feed is also provided with grease pre-heaters.
Further, also grease filter is provided with between described grease degasser discharge port and hydrolysis tower opening for feed.
Further, described higher pressure steam inlet adopts nozzle, realizes directly spraying into of steam.
Further, whipping appts is provided with in described hydrolysis tower.
The object of fat hydrolysis is grease to resolve into lipid acid and glycerine, and gained glycerol liquor concentration can reach about 15%, and its quality is high, impurity is few, is commonly called as " sugar water ".
The principle of work of the utility model soapmaking high pressure grease hydrolysis system: raw material enters grease degasser after heating in grease pre-heaters, complete the filtration of degassed raw material through grease filter, hydrolysis tower is squeezed into through grease high-pressure pump, be hydrolyzed in hydrolysis tower at the raw material that acts on of high pressure steam, the light constituent (lipid acid) obtained after hydrolysis enters in fatty water cooler and cools, and it is for subsequent use that the lipid acid that cooling obtains enters lipid acid subsider; The heavy constituent obtained after water quality enters sugar water flash tank, and the sugar water obtained squeezes into sugar water subsider through pump.
The utility model soapmaking high pressure grease hydrolysis system is simple and reasonable for structure, compact, can realize the hydrolysis of grease efficiently, fast; The utility model high pressure steam point multiply enters hydrolysis tower, can realize being uniformly distributed of high pressure steam, by controlling to pass into high pressure steam number of share of stock, controlled hydrolysis speed.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model soapmaking high pressure grease hydrolysis system.
Wherein
1-grease degasser; 2-hydrolysis tower; 3-lipid acid water cooler; 4-lipid acid subsider; 5-sugar water flash tank; 6-sugar water subsider; 7-grease pre-heaters; 8-grease filter; 9-interchanger.
Embodiment
Below in conjunction with embodiment, the utility model is further illustrated:
Embodiment 1
Present embodiment discloses a kind of soapmaking high pressure grease hydrolysis system, comprise grease degasser 1, hydrolysis tower 2, lipid acid water cooler 3, lipid acid subsider 4, sugar water flash tank 5, sugar water subsider 6 as shown in Figure 1; Described grease degasser 1 discharge port is communicated with hydrolysis tower 2 opening for feed, described hydrolysis tower 2 lower end products export is communicated with the feeding mouth of sugar water flash tank 5 upper end, the discharge port of described sugar water flash tank 5 lower end is communicated with sugar water subsider 6, described hydrolysis tower 2 upper end discharge port is communicated with lipid acid water cooler 3 upper end, described lipid acid water cooler 3 lower end discharge port is communicated with lipid acid subsider 4, described hydrolysis tower 2 sidewall upper is provided with 3 higher pressure steam inlet, described hydrolysis tower sidewall is also provided with condensation-water drain, for collecting the condensed water of condensation of high pressure steam.
Described grease degasser 1 opening for feed is also provided with grease pre-heaters 7.
Grease filter 8 is also provided with between described grease degasser 1 discharge port and hydrolysis tower 2 opening for feed.
Described higher pressure steam inlet adopts nozzle, realizes directly spraying into of steam.
Interchanger 9 is also provided with between described lipid acid water cooler 3 and lipid acid subsider 4
The principle of work of the soapmaking high pressure grease hydrolysis system that the present embodiment provides: raw material enters grease degasser 1 after heating in grease pre-heaters 7, complete the filtration of degassed raw material through grease filter 8, hydrolysis tower 2 is squeezed into through grease high-pressure pump, be hydrolyzed in hydrolysis tower 2 at the raw material that acts on of high pressure steam, the light constituent (lipid acid) obtained after hydrolysis enters in fatty water cooler 3 and cools, and it is for subsequent use that the lipid acid that cooling obtains enters lipid acid subsider 4; The heavy constituent obtained after water quality enters sugar water flash tank 5, and the sugar water obtained squeezes into sugar water subsider 6 through pump.
Embodiment 2
Soapmaking high pressure grease hydrolysis system disclosed in the present embodiment substantially the same manner as Example 1 unlike, described hydrolysis tower sidewall upper is provided with 5 higher pressure steam inlet, is provided with whipping appts in described hydrolysis tower.
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 soapmaking high pressure grease hydrolysis system, is characterized in that, comprises grease degasser, hydrolysis tower, lipid acid water cooler, lipid acid subsider, sugar water flash tank, sugar water subsider; Described grease degasser discharge port is communicated with hydrolysis tower opening for feed, described hydrolysis tower lower end products export is communicated with the feeding mouth of sugar water flash tank upper end, the discharge port of described sugar water flash tank lower end is communicated with sugar water subsider, described hydrolysis tower upper end discharge port is communicated with lipid acid water cooler upper end, described lipid acid water cooler lower end discharge port is communicated with lipid acid subsider, described hydrolysis tower sidewall upper is provided with more than 3 higher pressure steam inlet, and described hydrolysis tower sidewall is also provided with condensation-water drain.
2. according to claim 1 soapmaking high pressure grease hydrolysis system, it is characterized in that, described grease degasser opening for feed is also provided with grease pre-heaters.
3. according to claim 1 soapmaking high pressure grease hydrolysis system, it is characterized in that, between described grease degasser discharge port and hydrolysis tower opening for feed, be also provided with grease filter.
4. according to claim 1 soapmaking high pressure grease hydrolysis system, it is characterized in that, described higher pressure steam inlet adopts nozzle.
5. according to claim 1 soapmaking high pressure grease hydrolysis system, it is characterized in that, in described hydrolysis tower, be provided with whipping appts.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520097673.3U CN204455052U (en) | 2015-02-11 | 2015-02-11 | Soapmaking high pressure grease hydrolysis system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520097673.3U CN204455052U (en) | 2015-02-11 | 2015-02-11 | Soapmaking high pressure grease hydrolysis system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204455052U true CN204455052U (en) | 2015-07-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520097673.3U Expired - Fee Related CN204455052U (en) | 2015-02-11 | 2015-02-11 | Soapmaking high pressure grease hydrolysis system |
Country Status (1)
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| CN (1) | CN204455052U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105255594A (en) * | 2015-10-30 | 2016-01-20 | 杭州油脂化工有限公司 | Grease high-pressure hydrolysis production method and production device by recycling sweet water |
| CN105709462A (en) * | 2016-04-28 | 2016-06-29 | 南阳师范学院 | Degassing device used before high pressure hydrolysis of glycerol stearate |
| CN107354011A (en) * | 2017-08-30 | 2017-11-17 | 浙江嘉化能源化工股份有限公司 | Grease hydrolysis method |
| CN114561251A (en) * | 2022-03-09 | 2022-05-31 | 陕西海斯夫生物工程有限公司 | Convection hydrolysis tower and application thereof |
-
2015
- 2015-02-11 CN CN201520097673.3U patent/CN204455052U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105255594A (en) * | 2015-10-30 | 2016-01-20 | 杭州油脂化工有限公司 | Grease high-pressure hydrolysis production method and production device by recycling sweet water |
| CN105709462A (en) * | 2016-04-28 | 2016-06-29 | 南阳师范学院 | Degassing device used before high pressure hydrolysis of glycerol stearate |
| CN107354011A (en) * | 2017-08-30 | 2017-11-17 | 浙江嘉化能源化工股份有限公司 | Grease hydrolysis method |
| CN114561251A (en) * | 2022-03-09 | 2022-05-31 | 陕西海斯夫生物工程有限公司 | Convection hydrolysis tower and application thereof |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150708 Termination date: 20200211 |