CN108951256A - A kind of slurrying decatize transverse tube - Google Patents
A kind of slurrying decatize transverse tube Download PDFInfo
- Publication number
- CN108951256A CN108951256A CN201811157405.0A CN201811157405A CN108951256A CN 108951256 A CN108951256 A CN 108951256A CN 201811157405 A CN201811157405 A CN 201811157405A CN 108951256 A CN108951256 A CN 108951256A
- Authority
- CN
- China
- Prior art keywords
- spiral conveying
- tube
- decatize
- slurrying
- conveying tube
- 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.)
- Pending
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Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C7/00—Digesters
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
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- Materials For Medical Uses (AREA)
Abstract
The present invention provides a kind of slurrying decatize transverse tube, and slurrying decatize transverse tube is attached by connecting tube between spiral conveying tube including the spiral conveying tube that multistage is set side by side, steam vent and medicine feeding hole are provided on spiral conveying tube.Steam can be added in the slurrying decatize transverse tube, medical fluid is added, stalk is softened, carry out under normal pressure, reach bating effect, improve efficiency, saved the time.
Description
Technical field
The present invention relates to the devices that stalk is softened in pulping process, more particularly, to a kind of slurrying decatize transverse tube.
Background technique
At present for broken stalk, is softened using storehouse/container splendid attire, because wheat straw waste bulk density is low, storehouse easily occur
Interior bridging does not discharge, and influences to run.
Summary of the invention
The present invention provides a kind of slurrying decatize transverse tubes, solve the problems, such as that stalk is softened in the paper making process, no
Will appear stalk bridging influences transmission, and it is described that its technical solution is as follows:
A kind of slurrying decatize transverse tube passes through connection between spiral conveying tube including the spiral conveying tube that multistage is set side by side
Pipe is attached, and steam vent is provided on spiral conveying tube.
The steam vent is connected by steam pipe with steaming device, and it is 60 DEG C~100 DEG C that steam unit, which provides vapor (steam) temperature,.
The vapor (steam) temperature is 85 DEG C~100 DEG C.
The end of first order spiral conveying tube is connected by the first connecting tube with the end of second level spiral conveying tube, the
The head end of deuterostrophies delivery pipe is connected by the second connecting tube with the head end of third level spiral conveying tube, third level spiral transferring
It send the end of pipe to be connected by third connecting tube with the end of fourth stage spiral conveying tube, is sequentially connected backward.
The spiral conveying tube uses 2-4 grades.
Spiral conveying tube uses 2 grades, and the length of first order spiral conveying tube and second level spiral conveying tube is 6~11m.
The length of first order spiral conveying tube and second level spiral conveying tube is 9~10m.
Multiple coil delivery pipe is arranged in parallel or is arranged at any angle.
Steam vent, medicine feeding hole are provided in the connecting tube.
The effective connecting flange substitution of connection.
Steam can be added in the slurrying decatize transverse tube, addition medical fluid softens stalk, carry out under normal pressure, reach soft
Change effect, improves efficiency, saved the time.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of slurrying decatize transverse tube embodiment.
Specific embodiment
Slurrying decatize transverse tube provided by the invention, including the spiral conveying tube that is set side by side of multistage, between spiral conveying tube
It is attached by connecting tube, steam vent and medicine feeding hole is provided on spiral conveying tube.The end of first order spiral conveying tube is logical
It crosses the first connecting tube to be connected with the end of second level spiral conveying tube, the head end of second level spiral conveying tube passes through the second connection
Pipe is connected with the head end of third level spiral conveying tube, and the end of third level spiral conveying tube passes through third connecting tube and the fourth stage
The end of spiral conveying tube is connected, and is sequentially connected backward.
In embodiment in Fig. 1, two-stage screw delivery pipe is used, the structure of every grade of spiral conveying tube is identical, including
Motor, helical axis, tube wall, material inlet, material outlet and steam vent and medicine feeding hole, the material inlet are positioned close to motor
One end, the motor drive helical axis to be rotated, and then helical blade is driven to carry out material transmission.
First order spiral conveying tube 10 is provided with motor 11, helical axis 12, tube wall, material inlet 1, material outlet 3, steam vent
Or medicine feeding hole 2, second level spiral conveying tube 20 are provided with motor 21, helical axis 22, tube wall, material inlet 5, material outlet 4, vapour
Hole or medicine feeding hole.The first order spiral conveying tube 10 and second level spiral conveying tube 20 are arranged in parallel, and the material outlet 3 is logical
Connecting tube or connecting flange is crossed to be connected with material outlet 4, the transmission direction of first order spiral conveying tube 10 be from material into
For mouth 1 to material outlet 3, the transmission direction of second level spiral conveying tube 20 is from material outlet 4 to material inlet 5.
As it can be seen that in the spiral conveying tube that multistage is set side by side, transmission direction is successively opposite.
In use, first order spiral conveying tube 10 and second level spiral conveying tube 20 all use the spiral conveying tube of 10m long.
The vapor (steam) temperature of decatize is 80 DEG C -100 DEG C, steam vent, medicine feeding hole has been evenly arranged on spiral conveying tube, for passing
Defeated steam and drug.
In this way, softening the stalk after fine crushing.
The juxtaposition design of spiral conveying tube greatly reduces placement space in the present invention, and screw propulsion mode can be with side
Side stirring is conveyed, stalk can be crushed, and come into full contact with medical fluid with stalk.
Claims (10)
1. a kind of slurrying decatize transverse tube, it is characterised in that: including the spiral conveying tube that is set side by side of multistage, between spiral conveying tube
It is attached by connecting tube, steam vent is provided on spiral conveying tube.
2. slurrying decatize transverse tube according to claim 1, it is characterised in that: the steam vent passes through steam pipe and steaming device phase
Connection, it is 60 DEG C~100 DEG C that steam unit, which provides vapor (steam) temperature,.
3. slurrying decatize transverse tube according to claim 1, it is characterised in that: the vapor (steam) temperature is 85 DEG C~100 DEG C.
4. slurrying decatize transverse tube according to claim 1, it is characterised in that: the end of first order spiral conveying tube passes through the
One connecting tube is connected with the end of second level spiral conveying tube, the head end of second level spiral conveying tube by the second connecting tube with
The head end of third level spiral conveying tube is connected, and the end of third level spiral conveying tube passes through third connecting tube and fourth stage spiral
The end of delivery pipe is connected, and is sequentially connected backward.
5. slurrying decatize transverse tube according to claim 4, it is characterised in that: the spiral conveying tube uses 2-4 grades.
6. slurrying decatize transverse tube according to claim 5, it is characterised in that: spiral conveying tube uses 2 grades, first order spiral
Delivery pipe and the length of second level spiral conveying tube are 6~11m.
7. slurrying decatize transverse tube according to claim 6, it is characterised in that: first order spiral conveying tube and second level spiral
The length of delivery pipe is 9~10m.
8. slurrying decatize transverse tube according to claim 1, it is characterised in that: multiple coil delivery pipe be arranged in parallel or at appoint
Angle of anticipating setting.
9. slurrying decatize transverse tube according to claim 1, it is characterised in that: be provided with steam vent, dosing in the connecting tube
Hole.
10. -8 any slurrying decatize transverse tube according to claim 1, it is characterised in that: the effective connecting flange of connection
Substitution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811157405.0A CN108951256A (en) | 2018-09-30 | 2018-09-30 | A kind of slurrying decatize transverse tube |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811157405.0A CN108951256A (en) | 2018-09-30 | 2018-09-30 | A kind of slurrying decatize transverse tube |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108951256A true CN108951256A (en) | 2018-12-07 |
Family
ID=64472525
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811157405.0A Pending CN108951256A (en) | 2018-09-30 | 2018-09-30 | A kind of slurrying decatize transverse tube |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108951256A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110714351A (en) * | 2019-09-29 | 2020-01-21 | 山东世纪阳光纸业集团有限公司 | Process for pulping and papermaking of plant fiber in bio-mechanical or chemical-mechanical manner |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004005608A1 (en) * | 2002-07-02 | 2004-01-15 | Andritz, Inc. | Solvent pulping of biomass |
| CN101338529A (en) * | 2008-08-25 | 2009-01-07 | 王古宾 | High-pressure multi-tube continuous digester combined pulp grinder |
| WO2012147094A1 (en) * | 2011-03-25 | 2012-11-01 | Keswani, S.L. | Method and system for extraction of black liquor from a horizontal tube continuous digester |
| CN103132359A (en) * | 2013-03-26 | 2013-06-05 | 孟周强 | Transverse tube continuous cooking and steam explosion apparatus for biomass cellulosic ethanol |
| CN104611084A (en) * | 2015-01-19 | 2015-05-13 | 天津市天人世纪科技有限公司 | Method for producing clean energy material from agricultural and forestry waste |
| CN104790242A (en) * | 2015-04-09 | 2015-07-22 | 昌邑润德生态纤维有限公司 | Normal-pressure steaming bin and technology for treating material by utilizing same |
| CN106868909A (en) * | 2017-01-11 | 2017-06-20 | 杨太松 | It is a kind of can stop cleaning stalk cellulose high-pressure multi-tube continuous digester combined pulp grinder |
| CN108560300A (en) * | 2018-06-27 | 2018-09-21 | 刘同林 | One kind comprehensively utilizing pretreated continuously cooking system for stalk |
-
2018
- 2018-09-30 CN CN201811157405.0A patent/CN108951256A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004005608A1 (en) * | 2002-07-02 | 2004-01-15 | Andritz, Inc. | Solvent pulping of biomass |
| CN101338529A (en) * | 2008-08-25 | 2009-01-07 | 王古宾 | High-pressure multi-tube continuous digester combined pulp grinder |
| WO2012147094A1 (en) * | 2011-03-25 | 2012-11-01 | Keswani, S.L. | Method and system for extraction of black liquor from a horizontal tube continuous digester |
| CN103132359A (en) * | 2013-03-26 | 2013-06-05 | 孟周强 | Transverse tube continuous cooking and steam explosion apparatus for biomass cellulosic ethanol |
| CN104611084A (en) * | 2015-01-19 | 2015-05-13 | 天津市天人世纪科技有限公司 | Method for producing clean energy material from agricultural and forestry waste |
| CN104790242A (en) * | 2015-04-09 | 2015-07-22 | 昌邑润德生态纤维有限公司 | Normal-pressure steaming bin and technology for treating material by utilizing same |
| CN106868909A (en) * | 2017-01-11 | 2017-06-20 | 杨太松 | It is a kind of can stop cleaning stalk cellulose high-pressure multi-tube continuous digester combined pulp grinder |
| CN108560300A (en) * | 2018-06-27 | 2018-09-21 | 刘同林 | One kind comprehensively utilizing pretreated continuously cooking system for stalk |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110714351A (en) * | 2019-09-29 | 2020-01-21 | 山东世纪阳光纸业集团有限公司 | Process for pulping and papermaking of plant fiber in bio-mechanical or chemical-mechanical manner |
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