CN102797188A - Numerical control continuous steam explosion machine - Google Patents
Numerical control continuous steam explosion machine Download PDFInfo
- Publication number
- CN102797188A CN102797188A CN2011101475288A CN201110147528A CN102797188A CN 102797188 A CN102797188 A CN 102797188A CN 2011101475288 A CN2011101475288 A CN 2011101475288A CN 201110147528 A CN201110147528 A CN 201110147528A CN 102797188 A CN102797188 A CN 102797188A
- Authority
- CN
- China
- Prior art keywords
- pressure cylinder
- high pressure
- cylinder body
- steam explosion
- steam
- 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
Links
Images
Landscapes
- General Preparation And Processing Of Foods (AREA)
Abstract
The invention relates to production equipment for performing steam explosion pretreatment on biomass, in particular to pretreatment equipment in biomass utilization industry and provides a numerical control continuous steam explosion machine which can finish a supersonic speed steam explosion process in 8.75milliseconds according to a principle of a sliding sealing cover. The air bleeding section area of the steam explosion machine, namely the section area of the sliding sealing cover is equal to the section area of a high-pressure cylinder body, and the section area is in a fixed proportion with a steam explosion treatment volume, so that the problem that air bleeding time is prolonged along with the increasing of the treatment volume in the conventional hot blow process is solved, the power density of steam explosion is improved by three magnitude orders, the curing degrees of materials which are treated in batches are consistent, and the foundation is laid for the consistency of an industrial biochemical treatment process. Meanwhile, the machine has the fully-automatic feeding and discharging function, so that continuous steam explosion production is realized.
Description
Technical field
The present invention relates to a kind ofly living beings carried out the pretreated production equipment of steam explosive-crushing, the pre-processing device of the matter utilization industry of making a living.
Background technology
The technological essence of steam explosive-crushing (Steam Explosion) is: will infilter the inner sudden release of steam molecule short time of plant tissue and finish, purpose is with less energy raw material to be decomposed by purpose.Steam explosive machine be with the raw material in the container and high steam in the scope of Millisecond, be suspended in airspace with fried form of loosing.This process has not only been utilized the high pressure potential energy of steam, and main is to make internal steam work be converted into mechanical energy, has realized the adiabatic expansion acting.Because its action time is short; Energy density height and active position are concentrated; Make the stream molecule that is penetrated between the big molecule such as cellulose and lignin produce powerful destructive power, can on big molecular level, material be decomposed fully, for basic condition is created in biochemical treatments such as late enzyme hydrolysis.
The quick-fried equipment of present vapour can only be referred to as hot spraying device, and its basic model is: at a pressure vessel bottom device valve, realize that through opening fast of valve pressure discharges suddenly, produce heat and spurt effect.The subject matter that this pattern exists is: because the venting cross section is little a lot of with respect to the pressure vessel volume; And the high pressure valve opening speed is limited, and the pressure releasing process time of high steam is long, is generally 3～10 seconds; Be difficult to reach Millisecond; Can't realize the acting of steam adiabatic expansion, reduce energy density, make the material degree of decomposition not high.And when vessel volume strengthened, valve can't equal proportion amplify, and had more widened the gap of venting cross section and vessel volume, and pressure releasing process is prolonged further.Therefore this heat real steam explosive-crushing phenomenon of having spurted mode producing not.In addition, also have a kind of technology mode of simulating the steam explosive-crushing process through the continuous extrusion way of screw rod, be characterized in: solid content or title material dry body receive heavily stressed extruding and produce high temperature, and after its outlet extrusion stress disappeared, material was expanded.This technical process is not to infiltrate the inner mode of plant tissue with gas to fill the compression gas ability that can break out; And blast discharges in the short time to make it; Therefore do not possess the condition of " quick-fried ", do not have quick-fried sound yet, can't break original cellulose macromolecule lattice from molecular level.Consequently come compression solid, but do not produce the pretreated Expected Results of cellulosic material with huge power consumption, little for the enzyme hydrolysis help in later stage.
Summary of the invention
The objective of the invention is in order to overcome the deficiency of above-mentioned prior art, provide a kind of utilization slip capping principle can in the time of Millisecond (0.00875s), accomplish the continuous Steam explosive machine of numerical control of supersonic speed steam explosive-crushing process.The capping sectional area equals the high pressure cylinder body sectional area because the venting sectional area of this Steam explosive machine promptly slides; And this sectional area becomes fixed proportion with the quick-fried processing volume of vapour; This spurts the technology problem that deflation time prolongs with handling volume to strengthen with regard to having overcome traditional hot; Not only make the quick-fried power density of vapour improve three one magnitude, and material " living ripe " degree that mass is handled is consistent, for industrialization biochemical processing process uniformity is laid a good foundation.Simultaneously, these facility are equipped with the full-automatic feeding-discharging function, have realized the quick-fried production of serialization vapour.
The objective of the invention is to realize in the following manner:
The present invention includes: high pressure cylinder body, slip capping, automatic feeding system, recovery bin, framework, top feed bin, material receive storehouse, pneumatic system, digital control system.Wherein, the slip capping is set in the high pressure cylinder body, can slide up and down therein, realizes slipper seal through the private sealing assembly.When the slip capping when end operation puts in place, can realize the high pressure cylinder body port sealing; Can open port sealing when the slip capping to other end operation, the whole cross section of high pressure cylinder body is exposed in the atmosphere, thereby accomplish from being fed to the do action of producing.It is suitable for reading that automatic feeding system is installed on high pressure cylinder body, and the integral high pressure cylinder apparatus is in recovery bin top, and steam-out (SO) is passed in the high pressure cylinder body through pipeline.High pressure cylinder body, slip capping, recovery bin, top feed bin, material receive the storehouse, pneumatic system all is installed on framework inside.Digital control system is independent of outside the body, can carry out Long-distance Control.The course of work of the continuous Steam explosive machine of numerical control is such:
Under digital control system control, at first open the feeding cover at slip capping top and shift to a side by automatic feeding system, fall the pan feeding guide directly over the high pressure cylinder body again, the material in the framework upper feed bin is discharged in the high pressure cylinder body; After material is filled it up with, by automatic feeding system the pan feeding guide is packed up again, retract feeding cover and snap into slip capping top; Can open steam and get into valve this moment, makes steam get into high pressure cylinder body; After reaching predetermined pressure permeation equilibration time, steam off gets into valve, starts pneumatic system simultaneously; Driving slides to be sealed on does rectilinear motion downwards in the high pressure cylinder body; Cause slip capping upper and lower side compression area and do not wait, produce the pressure unstability and cause steam to launch, drive slip capping motion rapidly downwards; Thoroughly open the high pressure cylinder body cross section, and make the vapor mixing material of integral high pressure cylinder interior produce prominent quick-fried.Because slip capping size is suitable with the high pressure cylinder body internal diameter, this process has been simulated pressure vessel divided into two parts blast process suddenly fully, and it is long-pending that the sectional area of promptly exitting equals container section, guaranteed prominent the putting property that vapour is quick-fried from structural principle.Simultaneously, the opening process in venting cross section is to launch completion by the steam that steam self pressure reduction causes, and has also reached the speed of Millisecond.Driven by the huge impulse force of high steam outburst; Material moment is launched into recovery bin at a high speed; The effect of the conjuncted cyclone separator through recovery bin; Blast is separated, upwards discharge, produce material and then receive the storehouse and continuously pass out to next procedure by material transfer equipment to falling into material by exhaust outlet.
Advantage of the present invention is:
1, the quick-fried venting of vapour of the present invention cross section equals container section, has realized that at utmost outburst is sudden.Deflation time is limited by venting valve and container size in the phase specific heat spraying device, and deflation time of the present invention and vessel volume size are irrelevant, is guaranteeing to have got through technology channel for the quick-fried equipment of large-scale vapour under the constant prerequisite of the quick-fried effect of vapour.
2, the present invention quickens to drive the slip capping through the steam pressure unstability; It is huge that the steam that is produced launches the effect energy; Realize high-speed driving slip capping, its driving force is directly proportional with container section, make the slip capping no matter scale of construction quality size can both accomplish fast that vapour is quick-fried to be opened.
3, owing in the time of Millisecond, accomplish explosion, make water vapour carry out the adiabatic expansion acting, internal steam work is converted into mechanical energy and acts on living beings histocyte interlayer; Improved blasting energy density; Material is fully decomposed, make the steam dwell time shorten to tens seconds, also need not chemicals and add by tens minutes; Not only practice thrift the steam energy consumption, and improved the production capacity of equipment.
4, the present invention since all materials produce process and in the time of Millisecond, accomplish; Avoided in the hot spraying device first second cooking level different problems with the tenth second ejection material; I.e. " preceding ripe then give birth to " problem provides the preliminary treatment material of biochemical characteristic high unity for subsequent treatment.Satisfied process consistency requirement in the suitability for industrialized production.
5, operation overall process of the present invention goes out the pan feeding full-automation by computer numerical controlled operation, has realized continuous production.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the present invention is done further description.
Fig. 1 is the complete machine front view of one embodiment of the invention.
Fig. 2 removes for one embodiment of the invention that machine mandrel surveys view behind the shell.
Fig. 3 is the high pressure cylinder body cutaway view of one embodiment of the invention.
With reference to accompanying drawing, the present invention includes: high pressure cylinder body 1, slip capping 2, automatic feeding system 3, recovery bin 4, framework 5, top feed bin 6, material receive storehouse 7, pneumatic system 8, digital control system.
In Fig. 1 and Fig. 2 embodiment: it is suitable for reading that automatic feeding system 3 is installed on high pressure cylinder body 1, and integral high pressure cylinder body 1 is installed on recovery bin 4 tops, and steam is passed in the high pressure cylinder body 1 through pipeline.High pressure cylinder body 1, slip capping 2, recovery bin 4, top feed bin 6, material receive storehouse 7, pneumatic system 8 all is installed on framework 5 inside.Digital control system is independent of outside the body, can carry out Long-distance Control.In Fig. 3: slip capping 2 is set in the high pressure cylinder body 1, can slide up and down therein, realizes slipper seal through the private sealing assembly.When slip capping 2 when end operation puts in place, can realize high pressure cylinder body 1 port sealing; Can open port sealing when slip capping 2 to other end operation, high pressure cylinder body 1 whole cross section is exposed in the atmosphere, and accomplish from being fed to the do action of producing.
The course of work of the present invention is such: under digital control system control; At first open the feeding cover at slip capping 2 tops and shift to a side by automatic feeding system 3; Fall the pan feeding guide directly over the high pressure cylinder body 1 again, the materials in the framework upper feed bin 6 are discharged in the high pressure cylinder body 1; After material is filled it up with, by automatic feeding system 3 the pan feeding guide is packed up again, retract feeding cover and snap into slip capping 2 tops; Can open steam and get into valve this moment, makes steam get into high pressure cylinder body; After reaching predetermined pressure permeation equilibration time, steam off gets into valve, starts pneumatic system 8 simultaneously; Drive slip capping 2 and in high pressure cylinder body 1, do rectilinear motion downwards; Cause slip capping 2 upper and lower side compression areas and do not wait, produce the pressure unstability and cause steam to launch, drive slip capping 2 motion rapidly downwards; Thoroughly open the high pressure cylinder body cross section, and make the vapor mixing material of integral high pressure cylinder interior produce prominent quick-fried.Because slip capping 2 sizes are suitable with high pressure cylinder body 1 internal diameter, this process has been simulated pressure vessel divided into two parts blast process suddenly fully, and it is long-pending that the sectional area of promptly exitting equals container section, guaranteed prominent the putting property that vapour is quick-fried from structural principle.Simultaneously, the opening process in venting cross section is to launch completion by the steam that steam self pressure reduction causes, and has also reached the speed of Millisecond.Driven by the huge impulse force of high steam outburst; Material moment is launched into recovery bin 4 at a high speed; The effect of the conjuncted cyclone separator through recovery bin 4; Blast is separated, upwards discharge, produce material and then receive storehouse 7 and continuously pass out to next procedure by material transfer equipment to falling into material by exhaust outlet.
The specific embodiment
The continuous Steam explosive machine of LB-6 type numerical control is the practical implementation of foregoing invention.300 liters of every high pressure cylinder body volumes of this type Steam explosive machine, operating pressure 2.5Mpa, every cylinder per hour on average can be handled 1 ton of stalk or 3 ton-grain food, belong to medium-sized Steam explosive machine, generally are designed to the multi-cylinder paired running.For industry production such as biochemical industry, wine brewing, papermaking provide the continuous vapour of industrialization quick-fried preliminary treatment equipment.
Claims (1)
1. the continuous Steam explosive machine of numerical control comprises that high pressure cylinder body, slip capping, automatic feeding system, recovery bin, framework, top feed bin, material receive storehouse, pneumatic system, digital control system.Wherein, it is suitable for reading that automatic feeding system is installed on high pressure cylinder body, and the integral high pressure cylinder apparatus is in recovery bin top, and steam-out (SO) is passed in the high pressure cylinder body through pipeline.High pressure cylinder body, slip capping, recovery bin, top feed bin, material receive the storehouse, pneumatic system all is installed on framework inside.Digital control system is independent of outside the body, can carry out Long-distance Control.It is characterized in that: the slip capping is set in the high pressure cylinder body, and the slip capping can slide up and down in high pressure cylinder body, realizes slipper seal through the private sealing assembly; , slip when end operation puts in place, can realize the high pressure cylinder body port sealing in being sealed on high pressure cylinder body; Can open port sealing when the slip capping to other end operation, the whole cross section of high pressure cylinder body is exposed in the atmosphere, thereby accomplish from being fed to the do action of producing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011101475288A CN102797188A (en) | 2011-05-24 | 2011-05-24 | Numerical control continuous steam explosion machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011101475288A CN102797188A (en) | 2011-05-24 | 2011-05-24 | Numerical control continuous steam explosion machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102797188A true CN102797188A (en) | 2012-11-28 |
Family
ID=47196471
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011101475288A Pending CN102797188A (en) | 2011-05-24 | 2011-05-24 | Numerical control continuous steam explosion machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102797188A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103406336A (en) * | 2013-08-27 | 2013-11-27 | 天紫环保投资控股有限公司 | Steam ejection type organic waste disposer with feeding screw cap screwing function |
| CN103406339A (en) * | 2013-08-27 | 2013-11-27 | 天紫环保投资控股有限公司 | Steam ejection type organic waste disposer |
| CN103406335A (en) * | 2013-08-27 | 2013-11-27 | 天紫环保投资控股有限公司 | Pressure maintaining ejection device for steam ejection type organic waste disposer |
| CN104668274A (en) * | 2013-08-27 | 2015-06-03 | 天紫环保投资控股有限公司 | Steam catapult type organic garbage disposer with sliding guide ring |
| CN104668275A (en) * | 2013-08-27 | 2015-06-03 | 天紫环保投资控股有限公司 | Steam catapult type organic garbage disposer with limiting protection springs |
| CN104695256A (en) * | 2013-12-07 | 2015-06-10 | 刘翠红 | Quick-opening material feeding cover of steam blasting machine |
| CN104690077A (en) * | 2013-08-27 | 2015-06-10 | 天紫环保投资控股有限公司 | Gas-solid separating garbage disposal machine provided with sliding guiding rings |
| CN104692841A (en) * | 2013-08-27 | 2015-06-10 | 天紫环保投资控股有限公司 | Fertilizer preparation system of organic solid waste processor with limiting bevel edge |
| CN105728432A (en) * | 2013-08-27 | 2016-07-06 | 天紫环保投资控股有限公司 | Organic garbage disposal machine ejection steel cage based on sliding guide ring |
| CN112323528A (en) * | 2020-10-26 | 2021-02-05 | 中科慧农实业有限公司 | Biomass fiber separation device and use method thereof |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2701407A1 (en) * | 2009-04-23 | 2010-10-23 | Greenfield Ethanol Inc. | Fractionation of biomass for cellulosic ethanol and chemical production |
| CN201648837U (en) * | 2010-01-12 | 2010-11-24 | 张德云 | Energy-saving continuous steam explosion equipment |
| WO2010143307A1 (en) * | 2009-06-12 | 2010-12-16 | Katsuren Hisashi | Turbine device |
| CN201756659U (en) * | 2010-06-18 | 2011-03-09 | 广州华徽环保科技有限公司 | Continuous steam exploded machine for modification and activation on pure physics method molecule structure of straw fiber element |
| JP2011085125A (en) * | 2009-10-16 | 2011-04-28 | San World:Kk | Steam explosion engine |
| CN102059075A (en) * | 2010-11-25 | 2011-05-18 | 东南大学 | Piston supercharged material steam explosion method and device |
| CN102600763A (en) * | 2011-01-22 | 2012-07-25 | 于政道 | Numerically controlled continuous steam explosion machine |
-
2011
- 2011-05-24 CN CN2011101475288A patent/CN102797188A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2701407A1 (en) * | 2009-04-23 | 2010-10-23 | Greenfield Ethanol Inc. | Fractionation of biomass for cellulosic ethanol and chemical production |
| WO2010143307A1 (en) * | 2009-06-12 | 2010-12-16 | Katsuren Hisashi | Turbine device |
| JP2011085125A (en) * | 2009-10-16 | 2011-04-28 | San World:Kk | Steam explosion engine |
| CN201648837U (en) * | 2010-01-12 | 2010-11-24 | 张德云 | Energy-saving continuous steam explosion equipment |
| CN201756659U (en) * | 2010-06-18 | 2011-03-09 | 广州华徽环保科技有限公司 | Continuous steam exploded machine for modification and activation on pure physics method molecule structure of straw fiber element |
| CN102059075A (en) * | 2010-11-25 | 2011-05-18 | 东南大学 | Piston supercharged material steam explosion method and device |
| CN102600763A (en) * | 2011-01-22 | 2012-07-25 | 于政道 | Numerically controlled continuous steam explosion machine |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104690077A (en) * | 2013-08-27 | 2015-06-10 | 天紫环保投资控股有限公司 | Gas-solid separating garbage disposal machine provided with sliding guiding rings |
| CN103406339A (en) * | 2013-08-27 | 2013-11-27 | 天紫环保投资控股有限公司 | Steam ejection type organic waste disposer |
| CN103406335A (en) * | 2013-08-27 | 2013-11-27 | 天紫环保投资控股有限公司 | Pressure maintaining ejection device for steam ejection type organic waste disposer |
| CN104668274A (en) * | 2013-08-27 | 2015-06-03 | 天紫环保投资控股有限公司 | Steam catapult type organic garbage disposer with sliding guide ring |
| CN104668275A (en) * | 2013-08-27 | 2015-06-03 | 天紫环保投资控股有限公司 | Steam catapult type organic garbage disposer with limiting protection springs |
| CN103406336A (en) * | 2013-08-27 | 2013-11-27 | 天紫环保投资控股有限公司 | Steam ejection type organic waste disposer with feeding screw cap screwing function |
| CN104692841A (en) * | 2013-08-27 | 2015-06-10 | 天紫环保投资控股有限公司 | Fertilizer preparation system of organic solid waste processor with limiting bevel edge |
| CN103406336B (en) * | 2013-08-27 | 2015-10-07 | 天紫环保投资控股有限公司 | There is the Steam ejection type organic waste disposer that charging spiral cover screws function |
| CN103406339B (en) * | 2013-08-27 | 2016-01-06 | 天紫环保投资控股有限公司 | Steam ejection type organic waste disposer |
| CN103406335B (en) * | 2013-08-27 | 2016-03-02 | 天紫环保投资控股有限公司 | Steam ejection type organic waste disposer pressurize catapult-launching gear |
| CN105728432A (en) * | 2013-08-27 | 2016-07-06 | 天紫环保投资控股有限公司 | Organic garbage disposal machine ejection steel cage based on sliding guide ring |
| CN104695256A (en) * | 2013-12-07 | 2015-06-10 | 刘翠红 | Quick-opening material feeding cover of steam blasting machine |
| CN112323528A (en) * | 2020-10-26 | 2021-02-05 | 中科慧农实业有限公司 | Biomass fiber separation device and use method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102600763A (en) | Numerically controlled continuous steam explosion machine | |
| CN102797188A (en) | Numerical control continuous steam explosion machine | |
| CN105642188B (en) | Instantaneous ejection type Steam explosive machine | |
| CN103111231A (en) | Steam blasting machine | |
| CN102674909B (en) | Food waste hydrolysis and spray explosion system | |
| EP3293267B1 (en) | Method for processing a biomass containing lignocellulose | |
| EP2336344A1 (en) | Pre-treatment of cellulosic material | |
| Prosvirnikov et al. | Mechanization of continuous production of powdered cellulose technology | |
| CN103204712B (en) | Method for manufacturing fertilizer base materials from garbage containing organic matters | |
| CN104343030B (en) | The continuous pretreating process of lignocellulose-like biomass normal pressure | |
| CN101361588A (en) | Steam explosion technique testing desk | |
| CN102261005B (en) | Steam explosion device with double cylinders | |
| US10513823B2 (en) | Methods and devices for hydrothermal pretreatment of lignocellulosic biomass | |
| CN101331976B (en) | Tobacco low-temperature steam explosion expansion device and method | |
| CN203291824U (en) | Lignocellulose biomass raw material continuous steam explosion device | |
| CN105296329A (en) | Device and method for performing continuous pretreatment on lignocellulose material by utilizing microwave-diluted acid steam explosion | |
| CN203139981U (en) | Steam blasting machine | |
| CN202146757U (en) | Multi-port release steam explosion device | |
| CN206428510U (en) | A kind of gas Hong quick-fried processor | |
| CN202099647U (en) | Steam explosion device with double-cylinder structure | |
| EP2723849A1 (en) | An apparatus and method of processing microorganisms | |
| CN202688755U (en) | Energy storage type valve-opening device in steam explosion machine | |
| CN102206927A (en) | Method and device for blasting straw walls with oxygen | |
| CN215277198U (en) | Biomass blasting pressure release noise reduction buffer tank | |
| CN111286378A (en) | Rapid flash explosion equipment and method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20121128 |