CN204022790U - The production equipment of the high glycerine neat soap of a kind of high-moisture - Google Patents
The production equipment of the high glycerine neat soap of a kind of high-moisture Download PDFInfo
- Publication number
- CN204022790U CN204022790U CN201420331602.0U CN201420331602U CN204022790U CN 204022790 U CN204022790 U CN 204022790U CN 201420331602 U CN201420331602 U CN 201420331602U CN 204022790 U CN204022790 U CN 204022790U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- type heat
- pipeline
- production equipment
- neat soap
- 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.)
- Active
Links
Landscapes
- Detergent Compositions (AREA)
Abstract
The utility model relates to neat soap technical field, relate in particular to the production equipment of the high glycerine neat soap of a kind of high-moisture, comprise sour plate-type heat exchanger, alkali plate-type heat exchanger, dynamic mixer, neutralization reactor, soap base recycle pump, vacuum drier and extrusion machine, acid plate-type heat exchanger, alkali plate-type heat exchanger are connected with dynamic mixer by pipeline respectively, dynamic mixer, neutralization reactor, vacuum drier and extrusion machine are connected by pipeline successively, and soap base recycle pump is connected to bottom and the middle and upper part of neutralization reactor by two pipelines.Neat soap production equipment of the present utility model can be produced neat soap continuously, and production efficiency is high, improves the output of neat soap unit time, and cost is low, and constant product quality, can large-scale industrial production; The utility model adopts sour plate-type heat exchanger and alkali plate-type heat exchanger to improve temperature of reaction, and fast reaction speed does not re-use secondary mixer in neutralization reaction, saves energy consumption.
Description
Technical field
The utility model relates to neat soap technical field, relates in particular to the production equipment of the high glycerine neat soap of a kind of high-moisture.
Background technology
Soap is that the mankind use articles for washing with the longest history, and oneself has the history of thousands of years so far.Since 18th century, developing rapidly of several centuries passed through in soap industry, and to 20 middle of century, under the pressure of synthetic detergent fast development, soap output glides year by year.The market capacity atrophy gradually after reaching the historical output of the highest 1,800,000 tons in 1989 of soap series products, the basicly stable level ten thousand tons of 70-80 after 2000.In recent years, along with the growing interest of people to quality product and environmental safety, soap becomes again one of focus of concern.
While producing high-moisture, high glycerine neat soap, deionized water is to use different pumps to enter neutralization reactor by different pipelines with glycerine; Because glycerine viscosity is higher, poor fluidity, when production, use the more difficult neutralization reaction system that adds of rotor pump, and instability of flow, can only low yield produce; Can cause the high consumption of low yield, it is unstable that glycerine adds inhomogeneous quality.
Summary of the invention
The purpose of this utility model is to provide a kind of for the deficiencies in the prior art can produce continuously, the production equipment of the high glycerine neat soap of high-moisture of constant product quality.
To achieve these goals, the utility model adopts following technical scheme: the production equipment of the high glycerine neat soap of a kind of high-moisture, comprise sour plate-type heat exchanger, alkali plate-type heat exchanger, dynamic mixer, neutralization reactor, soap base recycle pump, vacuum drier and extrusion machine, acid plate-type heat exchanger, alkali plate-type heat exchanger are connected with dynamic mixer by pipeline respectively, dynamic mixer, neutralization reactor, vacuum drier and extrusion machine are connected by pipeline successively, and soap base recycle pump is connected to bottom and the middle and upper part of neutralization reactor by two pipelines.
Further, described sour plate-type heat exchanger is connected with lipid acid hold-up vessel by pipeline, and described alkali plate-type heat exchanger is connected with liquid caustic soda hold-up vessel and glycerin storage tank by pipeline respectively.
Further, described neutralization reactor is connected with additive charge pump by pipeline.
Further, described vacuum drier is connected with cyclonic separator by pipeline.
Further, described extrusion machine is connected with feed bin by pipeline.
Further, between described extrusion machine and feed bin, be provided with rotating blanking appts, the two ends of rotating blanking appts are connected with extrusion machine, feed bin respectively by pipeline.
Further, the bottom of described feed bin is connected with automatic packing machine by conveying belt.
Further, the top of described feed bin is connected with pneumatic ash handling device by pipeline.
The beneficial effects of the utility model are: neat soap production equipment of the present utility model can be produced neat soap continuously, and production efficiency is high, improve the output of neat soap unit time, and cost is low, and constant product quality, can large-scale industrial production; The utility model adopts sour plate-type heat exchanger and alkali plate-type heat exchanger to improve temperature of reaction, and fast reaction speed does not re-use secondary mixer in neutralization reaction, saves energy consumption.
brief description of the drawings:
Fig. 1 is structured flowchart of the present utility model.
Fig. 2 is structural representation of the present utility model.
Reference numeral is: 1-sour plate-type heat exchanger, 11-lipid acid hold-up vessel, 2-alkali plate-type heat exchanger, 21-liquid caustic soda hold-up vessel, 22-glycerin storage tank, 3-dynamic mixer, 4-neutralization reactor, 41-additive charge pump, 5-soap base recycle pump, 6-vacuum drier, 61-cyclonic separator, 7-extrusion machine, 71-feed bin, 72-rotating blanking appts, 73-automatic packing machine, 74-pneumatic ash handling device.
embodiment:
For the ease of those skilled in the art's understanding, be further described below in conjunction with embodiment and 1 ~ 2 pair of the utility model of accompanying drawing, the content that embodiment is mentioned is not to restriction of the present utility model.
See Fig. 1 ~ 2, the production equipment of the high glycerine neat soap of a kind of high-moisture, comprise sour plate-type heat exchanger 1, alkali plate-type heat exchanger 2, dynamic mixer 3, neutralization reactor 4, soap base recycle pump 5, vacuum drier 6 and extrusion machine 7, acid plate-type heat exchanger 1, alkali plate-type heat exchanger 2 are connected with dynamic mixer 3 by pipeline respectively, dynamic mixer 3, neutralization reactor 4, vacuum drier 6 and extrusion machine 7 are connected by pipeline successively, and soap base recycle pump 5 is connected to bottom and the middle and upper part of neutralization reactor 4 by two pipelines.
Lipid acid and liquid caustic soda (sodium hydroxide of concentration 45 ~ 50%) add first-stage dynamic mixing tank 3 to carry out neutralization reaction (level of response is 60% ~ 70%) through charging pump respectively, enter again neutralization reactor 4 and carry out complete neutralization reaction (level of response 100%) under 5 effects of soap base recycle pump, additive through pump delivery to neutralization reactor 4, it is mixed completely, the soap base reacting completely enters vacuum drier 6 with certain pressure and sprays into vacuum drier 6 by the shower nozzle rotating, amass at vacuum drier 6 inwalls so that thin solid state is attached, by scraper, dry and cooling soap-film are scraped from vacuum drier 6 inwalls, fall into extrusion machine 7 augers, through two-stage, particle is cut in extruding.
Neat soap production equipment of the present utility model can be produced neat soap continuously, and production efficiency is high, improves the output of neat soap unit time, and cost is low, and constant product quality, can large-scale industrial production; The utility model adopts sour plate-type heat exchanger 1 and alkali plate-type heat exchanger 2 to improve temperature of reaction, and fast reaction speed does not re-use secondary mixer in neutralization reaction, saves energy consumption.
In the present embodiment, described sour plate-type heat exchanger 1 is connected with lipid acid hold-up vessel 11 by pipeline, and described alkali plate-type heat exchanger 2 is connected with liquid caustic soda hold-up vessel 21 and glycerin storage tank 22 by pipeline respectively.Lipid acid hold-up vessel 11 is for lipid acid is provided, and liquid caustic soda hold-up vessel 21 and glycerin storage tank 22 are respectively used to provide liquid caustic soda and glycerine.
In the present embodiment, described neutralization reactor 4 is connected with additive charge pump 41 by pipeline.Additive charge pump 41 is for adding additive.
In the present embodiment, described vacuum drier 6 is connected with cyclonic separator 61 by pipeline.Cyclonic separator 61 can be isolated soap powder.
In the present embodiment, described extrusion machine 7 is connected with feed bin 71 by pipeline.Feed bin 71 is for storing neat soap.
In the present embodiment, between described extrusion machine 7 and feed bin 71, be provided with rotating blanking appts 72, the two ends of rotating blanking appts 72 are connected with extrusion machine 7, feed bin 71 respectively by pipeline.Rotating blanking appts 72 is for carrying from top to bottom neat soap.
In the present embodiment, the bottom of described feed bin 71 is connected with automatic packing machine 73 by conveying belt.Automatic packing machine 73 is for packing neat soap.
In the present embodiment, the top of described feed bin 71 is connected with pneumatic ash handling device 74 by pipeline.Pneumatic ash handling device 74 is for removing dust.
Above-described embodiment is preferably implementation of the utility model, and in addition, the utility model can also be realized by alternate manner, and any apparent replacement is all within protection domain of the present utility model without departing from the concept of the premise utility.
Claims (8)
1. the production equipment of the high glycerine neat soap of high-moisture, it is characterized in that: comprise sour plate-type heat exchanger, alkali plate-type heat exchanger, dynamic mixer, neutralization reactor, soap base recycle pump, vacuum drier and extrusion machine, acid plate-type heat exchanger, alkali plate-type heat exchanger are connected with dynamic mixer by pipeline respectively, dynamic mixer, neutralization reactor, vacuum drier and extrusion machine are connected by pipeline successively, and soap base recycle pump is connected to bottom and the middle and upper part of neutralization reactor by two pipelines.
2. the production equipment of the high glycerine neat soap of a kind of high-moisture according to claim 1, it is characterized in that: described sour plate-type heat exchanger is connected with lipid acid hold-up vessel by pipeline, described alkali plate-type heat exchanger is connected with liquid caustic soda hold-up vessel and glycerin storage tank by pipeline respectively.
3. the production equipment of the high glycerine neat soap of a kind of high-moisture according to claim 1, is characterized in that: described neutralization reactor is connected with additive charge pump by pipeline.
4. the production equipment of the high glycerine neat soap of a kind of high-moisture according to claim 1, is characterized in that: described vacuum drier is connected with cyclonic separator by pipeline.
5. the production equipment of the high glycerine neat soap of a kind of high-moisture according to claim 1, is characterized in that: described extrusion machine is connected with feed bin by pipeline.
6. the production equipment of the high glycerine neat soap of a kind of high-moisture according to claim 5, is characterized in that: between described extrusion machine and feed bin, be provided with rotating blanking appts, the two ends of rotating blanking appts are connected with extrusion machine, feed bin respectively by pipeline.
7. the production equipment of the high glycerine neat soap of a kind of high-moisture according to claim 5, is characterized in that: the bottom of described feed bin is connected with automatic packing machine by conveying belt.
8. the production equipment of the high glycerine neat soap of a kind of high-moisture according to claim 5, is characterized in that: the top of described feed bin is connected with pneumatic ash handling device by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420331602.0U CN204022790U (en) | 2014-06-20 | 2014-06-20 | The production equipment of the high glycerine neat soap of a kind of high-moisture |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420331602.0U CN204022790U (en) | 2014-06-20 | 2014-06-20 | The production equipment of the high glycerine neat soap of a kind of high-moisture |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204022790U true CN204022790U (en) | 2014-12-17 |
Family
ID=52062682
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420331602.0U Active CN204022790U (en) | 2014-06-20 | 2014-06-20 | The production equipment of the high glycerine neat soap of a kind of high-moisture |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204022790U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105151792A (en) * | 2015-09-17 | 2015-12-16 | 上海制皂(集团)如皋有限公司 | Soap grain air-conveying system device |
| CN105695189A (en) * | 2016-04-06 | 2016-06-22 | 青岛金牛化学有限公司 | Automatic continuous configuration device for animal oil fatty acid soap |
| CN115069184A (en) * | 2022-05-31 | 2022-09-20 | 南通联升电力科技有限公司 | Continuous saponification control system based on distributed IO |
-
2014
- 2014-06-20 CN CN201420331602.0U patent/CN204022790U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105151792A (en) * | 2015-09-17 | 2015-12-16 | 上海制皂(集团)如皋有限公司 | Soap grain air-conveying system device |
| CN105695189A (en) * | 2016-04-06 | 2016-06-22 | 青岛金牛化学有限公司 | Automatic continuous configuration device for animal oil fatty acid soap |
| CN115069184A (en) * | 2022-05-31 | 2022-09-20 | 南通联升电力科技有限公司 | Continuous saponification control system based on distributed IO |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204022790U (en) | The production equipment of the high glycerine neat soap of a kind of high-moisture | |
| CN204058428U (en) | A kind of neat soap production equipment | |
| CN204643043U (en) | A kind of dust-precipitating system for biomass material Belt Conveying | |
| CN203829925U (en) | Improved type modularized membrane separation equipment | |
| CN206137163U (en) | Improve equipment of filling material packing success rate in food processing | |
| CN203778041U (en) | High-efficiency continuous sulfur melting kettle | |
| CN103374464A (en) | Method for producing clean jelly glue | |
| CN204770678U (en) | Equipment of production indium pearl | |
| CN204246850U (en) | A kind of paraffin oil and the accurate separation system device of carrene | |
| CN204888074U (en) | Huge fungus grass cutting conveyor that production furfural was used | |
| CN204051390U (en) | For nitrocotton smoke of gunpowder recovery system | |
| CN201615685U (en) | Flash evaporation drier | |
| CN203140002U (en) | Reactor for producing ultrahigh-molecular-weight water-soluble polymer | |
| CN202621150U (en) | Isooctyl thioglycolate esterification kettle | |
| CN203602527U (en) | Stearate production device | |
| CN203540086U (en) | Device for removing dioxane of ethoxylated alkyl sulfate by centrifugal spraying | |
| CN208217809U (en) | A kind of feeder for medicine production | |
| CN204933553U (en) | A kind of granulation all-in-one | |
| CN204914310U (en) | High performance is deciduate cylinder of granulator for petroleum resin | |
| CN204891825U (en) | Hydrogenation ware | |
| CN208199704U (en) | It is a kind of to prepare oil well additive feeder | |
| CN207631972U (en) | A kind of feed device of processing processed soybean food | |
| CN204051021U (en) | A kind of water replenishing type thin film evaporator | |
| CN202516661U (en) | Grinder with condensers | |
| CN203873717U (en) | Mop washing device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 523000 New Town Industrial Park, Ma Chung, Dongguan, Guangdong Patentee after: Fengyi oil technology (Dongguan) Co., Ltd. Address before: 523147 fengsha oil chemical (Dongguan) Co., Ltd., Xin Sha Industrial Park, Ma Chung, Dongguan, Guangdong Patentee before: Fengyi oil chemical (Dongguan) Co., Ltd. |
|
| CP03 | Change of name, title or address |