CN201294832Y - High pressure charging device for function sugar alcohol production - Google Patents
High pressure charging device for function sugar alcohol production Download PDFInfo
- Publication number
- CN201294832Y CN201294832Y CNU2008202258535U CN200820225853U CN201294832Y CN 201294832 Y CN201294832 Y CN 201294832Y CN U2008202258535 U CNU2008202258535 U CN U2008202258535U CN 200820225853 U CN200820225853 U CN 200820225853U CN 201294832 Y CN201294832 Y CN 201294832Y
- Authority
- CN
- China
- Prior art keywords
- pump
- measuring tank
- high pressure
- liquid glucose
- sugar alcohol
- 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
This utility model discloses a high pressure charging device for function sugar alcohol production, belonging to the production field of the function sugar alcohol, including a decoloring sugar liquor storage tank, a sugar liquor measuring tank, a catalyst measuring tank and a reaction kettle. A connected conduit between the decoloring sugar liquor storage tank and the sugar liquor measuring tank is provided with a sugar liquor pump. A connected conduit between the sugar liquor measuring tank and the reaction kettle is provided with a conduit pump and a high pressure pump. A connected conduit between the catalyst measuring tank and the reaction kettle is provided with a secondary catalyst pump. Compared with the current technology, the high pressure charging device for function sugar alcohol production of this utility model has the advantages of reasonable structure, low manufacturing cost and simple operation, and it can save the energy and reduce the labor intensity.
Description
Technical field
The utility model relates to a kind of functional sugar alcohol production field, the high pressure charging of functional sugar alcohol production specifically device.
Background technology
Functional sugar alcohol such as xylitol, maltitol, sorbierite are to be raw material with wood sugar, maltose, glucose, through changing sugared hydrogenation, are separately converted to functional sugar alcohol such as xylitol, maltitol, sorbierite.Function sugar hydrogenation is to carry out under the effect of HTHP and catalyst, catalyst and liquid glucose charging, a lot of different feeding manners are arranged, need before the charging air in the reactor is discharged, charging is preceding the hydrogen emptying in the reactor, or be discharged in the preceding holding vessel of hydrogen pressure machine, the hydrogen pressure machine repeats the pressurization acting, causes the consumption of the waste or the energy.
Summary of the invention
Technical assignment of the present utility model is at above weak point, provide a kind of rational in infrastructure, production cost is low, the functional sugar alcohol production high pressure charging device of simple to operate, energy savings.
The technical scheme that its technical problem that solves the utility model adopts is: this device comprises decolouring liquid glucose storage tank, the liquid glucose measuring tank, catalyst measuring tank and reactor, the pipeline that is communicated with between decolouring liquid glucose storage tank and the liquid glucose measuring tank is provided with the liquid glucose pump, and the pipeline that is communicated with between liquid glucose measuring tank and the reactor is provided with tubing pump and high-pressure pump; The pipeline that is communicated with between catalyst measuring tank and the reactor is provided with quadric catalysis agent pump.
Described liquid glucose pump, quadric catalysis agent pump and high-pressure pump all respectively are provided with two.
During work, open tubing pump, high-pressure pump begins charging in reactor, open the catalyst measuring pump simultaneously and begin into catalyst, advance the amount of catalyst, by the liquid level control of catalyst measuring tank, catalyst stops the catalyst measuring pump after advancing the amount of enough stills, and catalyst charge stops.After the liquid level of liquid glucose measuring tank reaches needed inlet amount, stop high-pressure pump, tubing pump, charging stops, and reactor begins to enter down the operation in step.The charging of reactor only need be controlled inlet amount, and the hydrogen in the reactor does not need emptying, does not need to enter hydrogen-holder yet.
Functional sugar alcohol production high pressure charging device of the present utility model is compared with prior art, catalyst and liquid glucose add in the reactor simultaneously, operate fairly simple, both reduced the amount of labour of arranging hydrogen again behind operative employee's discharge, again hydrogen has been carried out reasonable use, the reacting kettle inner pressure height has reduced the acting intensity of hydrogen gas compressor, has saved the energy and labour to a great extent.
Description of drawings
Below in conjunction with accompanying drawing the utility model is further specified.
Accompanying drawing is the structural representation of functional sugar alcohol production high pressure charging device.
Among the figure: 1, decolouring liquid glucose storage tank, 2, the liquid glucose pump, 3, the liquid glucose measuring tank, 4, the catalyst measuring tank, 5, tubing pump, 6, quadric catalysis agent pump, 7, high-pressure pump, 8, reactor.
The specific embodiment
The utility model is described in further detail below in conjunction with the drawings and specific embodiments.
Functional sugar alcohol production high pressure charging device of the present utility model, its structure comprises decolouring liquid glucose storage tank 1, liquid glucose measuring tank 3, catalyst measuring tank 4 and reactor 8, the pipeline that is communicated with between decolouring liquid glucose storage tank 1 and the liquid glucose measuring tank 3 is provided with the liquid glucose pump 2 of two parallel connections, and the pipeline that is communicated with between liquid glucose measuring tank 3 and the reactor 8 is provided with the high-pressure pump 7 of tubing pump 5 and two parallel connections; The pipeline that is communicated with between catalyst measuring tank 4 and the reactor 8 is provided with the quadric catalysis agent pump 6 of two parallel connections.
Its processing and fabricating of functional sugar alcohol production high pressure charging device of the present utility model is very simple and convenient, and processing and fabricating gets final product shown in the by specification accompanying drawing.
Except that the described technical characterictic of specification, be the known technology of those skilled in the art.
Claims (2)
1, functional sugar alcohol production high pressure charging device, comprise decolouring liquid glucose storage tank, the liquid glucose measuring tank, catalyst measuring tank and reactor, the pipeline that is communicated with between liquid glucose storage tank and the liquid glucose measuring tank that it is characterized in that decolouring is provided with the liquid glucose pump, and the pipeline that is communicated with between liquid glucose measuring tank and the reactor is provided with tubing pump and high-pressure pump; The pipeline that is communicated with between catalyst measuring tank and the reactor is provided with quadric catalysis agent pump.
2, functional sugar alcohol production high pressure charging device according to claim 1 is characterized in that liquid glucose pump, quadric catalysis agent pump and high-pressure pump all respectively are provided with two.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202258535U CN201294832Y (en) | 2008-11-19 | 2008-11-19 | High pressure charging device for function sugar alcohol production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202258535U CN201294832Y (en) | 2008-11-19 | 2008-11-19 | High pressure charging device for function sugar alcohol production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201294832Y true CN201294832Y (en) | 2009-08-26 |
Family
ID=41040784
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008202258535U Expired - Fee Related CN201294832Y (en) | 2008-11-19 | 2008-11-19 | High pressure charging device for function sugar alcohol production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201294832Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105797665A (en) * | 2014-12-29 | 2016-07-27 | 中国石油天然气股份有限公司 | Liquefied petroleum gas anhydrous fracturing fluid preparation device and preparation method |
| CN110683936A (en) * | 2019-11-22 | 2020-01-14 | 浙江华康药业股份有限公司 | Pressure feeding damping device and sugar alcohol production line thereof |
-
2008
- 2008-11-19 CN CNU2008202258535U patent/CN201294832Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105797665A (en) * | 2014-12-29 | 2016-07-27 | 中国石油天然气股份有限公司 | Liquefied petroleum gas anhydrous fracturing fluid preparation device and preparation method |
| CN105797665B (en) * | 2014-12-29 | 2018-03-13 | 中国石油天然气股份有限公司 | Liquefied petroleum gas anhydrous fracturing fluid preparation device and preparation method |
| CN110683936A (en) * | 2019-11-22 | 2020-01-14 | 浙江华康药业股份有限公司 | Pressure feeding damping device and sugar alcohol production line thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201294832Y (en) | High pressure charging device for function sugar alcohol production | |
| CN201295607Y (en) | Device capable of reducing sugar liquid hydrogenation feed pressure and recycling hydrogen gas | |
| CN202490455U (en) | Vacuum buffer tank | |
| CN101225323B (en) | Method for preparing biodiesel from raw material by overcritical extraction-transesterification coupling process | |
| CN201420073Y (en) | High-hydraulic-pressure soft methane tank | |
| CN203602368U (en) | Spherical nickel hydroxide continuous synthesis device | |
| CN106190811A (en) | A kind of diphasic anaerobic fermentation is from stirring reaction unit | |
| CN205905450U (en) | Novel disk oil press | |
| CN201933069U (en) | Decompression type biodiesel preparing device | |
| CN201543379U (en) | Device capable of efficiently separating carbon dioxide from hydrogen | |
| CN203545989U (en) | Saccharification and fermentation tank | |
| CN201538688U (en) | Quantitative yellow phosphorus feeding device | |
| CN203741310U (en) | Fermentation tank for fruit vinegar production | |
| CN204569411U (en) | A kind of alcohols vapor reforming hydrogen production device | |
| CN201161920Y (en) | Bottoms material lift apparatus | |
| CN201825901U (en) | Production device for heparin sodium medicine | |
| CN201279455Y (en) | Device for replacing hydrogen using steam | |
| CN204869734U (en) | Super peanut oil that at present presses of merchant is with full -automatic hydraulic pressure accuse oil pressure squeezer | |
| CN201410309Y (en) | Avermectin extracting tank | |
| CN201551988U (en) | Device for preparing oxidized cellulose | |
| CN203820664U (en) | Production system of 2-chlorine-4-amino-toluene | |
| CN201292350Y (en) | Novel biodiesel production apparatus | |
| CN201962225U (en) | Decolorizing device in allantoin preparation process | |
| CN203593710U (en) | Reaction device used for preparing L-carnitine | |
| CN201880397U (en) | Device for recycling secondary-discolored active carbon |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090826 Termination date: 20111119 |