CN205569873U - Multistage siphon separator that hydrolysises of living beings - Google Patents
Multistage siphon separator that hydrolysises of living beings Download PDFInfo
- Publication number
- CN205569873U CN205569873U CN201620327592.2U CN201620327592U CN205569873U CN 205569873 U CN205569873 U CN 205569873U CN 201620327592 U CN201620327592 U CN 201620327592U CN 205569873 U CN205569873 U CN 205569873U
- Authority
- CN
- China
- Prior art keywords
- drainage tube
- buffering ball
- mozzle
- multistage
- hydrolysis
- 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
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a multistage siphon separator that hydrolysises of living beings, it is including inhaleing pipe (2), drainage tube (4), honeycomb duct (10) and buffering ball (7), dog -house (9) and gas vent (8) are established in buffering ball (7), honeycomb duct (10) is connected to the bottom of buffering ball (7), install honeycomb duct valve (11) on honeycomb duct (10), drainage tube (4) one end is connected at the top of buffering ball (7), install drainage tube valve (6) on drainage tube (4), establish blow vent (5) on drainage tube (4), suction pipe (2) is connected through adapter (3) to drainage tube (4) other end. The utility model discloses simple structure, convenient operation, the running cost is low, has the good result to the solid -liquid separation in the multistage hydrolytic process of living beings.
Description
Technical field
This utility model relates to biomass field of chemical equipment, specifically, relates to a kind of biomass multistage hydrolysis siphon segregation apparatus.
Background technology
Biomass material is hydrolyzed and can obtain numerous chemical products and energy substitution product.Hydrolysis process is generally divided into acid hydrolysis and enzyme hydrolysis by the difference of catalyst, is divided into again one-stage hydrolysis and multistage hydrolysis by the difference of hydrolysis number of times.Multi-level water solution preocess generally with mineral acid or enzyme as catalyst, uses repeatedly hydrolysis process, and more thoroughly, in hydrolyzed solution, production concentration is higher for substrate hydrolysis, and efficiency of pcr product is the highest.
Multi-level water solution preocess needs to carry out solid-liquid after hydrolysis terminates initial gross separation every time, then carries out next stage hydrolysis.Solid-liquid separation process typically requires a reactant and discharges from hydrolytic reaction pot, then is centrifuged or filter press, and gained solid content again puts into reactor and carries out next stage hydrolysis, operates complex, and production cost is the highest.
Summary of the invention
The purpose of this utility model is: design a kind of biomass multistage hydrolysis siphon segregation apparatus, simplifies the operation of biomass multistage hydrolytic process solid-liquid separation, reduces into product cost.
For achieving the above object, the technical solution of the utility model is: this biomass multistage hydrolysis siphon segregation apparatus includes suction tube, drainage tube, mozzle and buffering ball, buffering ball sets dog-house and air vent, the bottom of buffering ball connects mozzle, installing mozzle valve on mozzle, the top of buffering ball connects drainage tube one end, and drainage tube is installed drainage tube valve, setting blow vent on drainage tube, the drainage tube other end connects suction tube through adaptor.
Wherein, the pipe end of suction tube installs porous filter.
Advantage of the present utility model and having the beneficial effects that:
1, utilize buffering ball Inner guide liquid stream become homeless formed negative pressure make hydrolyzed solution constantly enter from suction tube, it is achieved solid-liquid separation；Meanwhile, in order to prevent pipeline blockage, close drainage tube valve, introduce gas from drainage tube blow vent and recoil；For high viscosity or high concentration fluid, the air vent on buffering ball connects vacuum pump to increase siphon separating effect.
2, this utility model simple in construction, easy to operate, operating cost is low, has good result for the solid-liquid separation in biomass multistage hydrolytic process.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1 porous filter；2 suction tubes；3 adaptors；4 drainage tubes；5 blow vents；6 drainage tube valves；7 buffering balls；8 air vents；9 dog-houses；10 mozzles；11 mozzle valves.
Detailed description of the invention
Below in conjunction with accompanying drawing, this utility model is further described.It is only used for clearly illustrating the technical solution of the utility model, and protection domain of the present utility model can not be limited with this.
As shown in Figure 1, this biomass multistage hydrolysis siphon segregation apparatus includes suction tube 2, drainage tube 4, mozzle 10 and buffering ball 7, buffering ball 7 sets dog-house 9 and air vent 8, the bottom of buffering ball 7 connects mozzle 10, installing mozzle valve 11 on mozzle 10, the top of buffering ball 7 connects drainage tube 4 one end, and drainage tube 4 is installed drainage tube valve 6, setting blow vent 5 on drainage tube 4, drainage tube 4 other end connects suction tube 2 through adaptor 3.
Wherein, the pipe end of suction tube 2 installs porous filter 1.
During work, porous filter 1 is placed in below biomass hydrolysate liquid level；Dog-house is closed after the dog-house 9 of buffering ball 7 adds diversion fluid, turn off the blow vent 5 of drainage tube 4 and the air vent 8 of buffering ball 7, open drainage tube valve 6 and mozzle valve 11, diversion fluid flows out because of action of gravity, the negative pressure formed in buffering ball 7 makes hydrolyzed solution constantly enter from porous filter 1, it is achieved siphon separates；Meanwhile, in order to prevent blocking, close drainage tube valve 6, introduce gas from the blow vent 5 of drainage tube 4 and recoil；For high viscosity or high concentration fluid, such as enzyme hydrolysis sugar liquid, the air vent 8 of buffering ball 7 connects vacuum pump to increase siphon separating effect.
The above is only preferred implementation of the present utility model; should be understood that; for those skilled in the art; on the premise of without departing from this utility model know-why; can also make some improvements and modifications, these improvements and modifications also should be regarded as protection domain of the present utility model.
Claims (2)
1. biomass multistage hydrolysis siphon segregation apparatus, it is characterized in that: it includes suction tube (2), drainage tube (4), mozzle (10) and buffering ball (7), buffering ball (7) sets dog-house (9) and air vent (8), the bottom of buffering ball (7) connects mozzle (10), mozzle (10) is upper installs mozzle valve (11), the top of buffering ball (7) connects drainage tube (4) one end, drainage tube (4) is upper installs drainage tube valve (6), blow vent (5) is set on drainage tube (4), drainage tube (4) other end connects suction tube (2) through adaptor (3).
Biomass multistage the most according to claim 1 hydrolysis siphon segregation apparatus, is characterized in that: suction tube (2) pipe end installs porous filter (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620327592.2U CN205569873U (en) | 2016-04-19 | 2016-04-19 | Multistage siphon separator that hydrolysises of living beings |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620327592.2U CN205569873U (en) | 2016-04-19 | 2016-04-19 | Multistage siphon separator that hydrolysises of living beings |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205569873U true CN205569873U (en) | 2016-09-14 |
Family
ID=56863299
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620327592.2U Expired - Fee Related CN205569873U (en) | 2016-04-19 | 2016-04-19 | Multistage siphon separator that hydrolysises of living beings |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205569873U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019033785A1 (en) * | 2017-08-16 | 2019-02-21 | 朱伟明 | Pipeline fluid flow velocity increasing method and pipeline fluid conveying system |
-
2016
- 2016-04-19 CN CN201620327592.2U patent/CN205569873U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019033785A1 (en) * | 2017-08-16 | 2019-02-21 | 朱伟明 | Pipeline fluid flow velocity increasing method and pipeline fluid conveying system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204474409U (en) | Rectilinear anaerobic aerobic integratedization reactor | |
| CN101811936B (en) | Benzyl alcohol continuous hydrolysis technology and use equipment thereof | |
| CN205569873U (en) | Multistage siphon separator that hydrolysises of living beings | |
| CN201593028U (en) | Device used in benzyl alcohol continuous hydrolysis technique | |
| CN201458785U (en) | Purified acid wastewater degasser | |
| CN201823402U (en) | Air and water automatic separator matched with water ring vacuum pump | |
| CN203998986U (en) | A kind of device of controlling alumina high temperature stripping organism and sulphur | |
| CN201565160U (en) | Anaerobic methane gas-liquid separation deaeration device | |
| CN203683208U (en) | MBR (membrane biological reactor) sewage treatment device | |
| CN104912802A (en) | Novel liquid loop vacuum pump system | |
| CN204961335U (en) | Water ring vacuum pump device | |
| CN201873536U (en) | Device for treating dust collecting slag generated in production of titanium tetrachloride | |
| CN208266238U (en) | A kind of biological oxidation gold extraction system circulation whirlwind defoaming device | |
| CN103011405A (en) | Artificial inner gas stripping anaerobic reactor | |
| CN204816199U (en) | Peace and quiet useless sodium hypochlorite of acetylene takes off and analyses acetylene gas purifier | |
| CN210699439U (en) | SO removal in reagent sulfuric acid production2In a device | |
| CN209778349U (en) | Air stripping adds medicine reflux unit | |
| CN204380493U (en) | A kind of dusty gas cleaning system for power industry high reactivity | |
| CN203754662U (en) | Methane gas-water separator | |
| CN204783671U (en) | Novel liquid ring vacuum pump system | |
| CN104906874A (en) | Automatic gas-liquid separation device and method for chlorine dioxide generator under high negative pressure environment | |
| CN108315554A (en) | A kind of biological oxidation gold extraction system circulation whirlwind defoaming device | |
| CN216005544U (en) | Sewage anaerobic treatment device | |
| CN204380496U (en) | A kind of low-loss high efficiency power industry dusty gas cleaning system | |
| CN204550195U (en) | EGSB anaerobic sludge refluxing reactor |
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: 20160914 Termination date: 20170419 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |