CN205170723U - Device of different appearance characteristic acetylation wood fibre materials of coproduction - Google Patents
Device of different appearance characteristic acetylation wood fibre materials of coproduction Download PDFInfo
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- CN205170723U CN205170723U CN201520910163.3U CN201520910163U CN205170723U CN 205170723 U CN205170723 U CN 205170723U CN 201520910163 U CN201520910163 U CN 201520910163U CN 205170723 U CN205170723 U CN 205170723U
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Abstract
The utility model relates to a device of different appearance characteristic acetylation wood fibre materials of coproduction is aimed at providing in wood working and protection field. The device includes first container and the inclosed second container of ability as the reactor, the second container is installed in the top of first container, inner space intercommunication between them to the baffle of having laid a plurality of apertures is as the interval, gaseous and liquid can freely pass through the aperture, and powdered or fibrous wood fibre material then can can not be passed through by the separation, heating device is established to first container outside cover, and the radiation shield casing is established to second container outside cover. Through using the utility model discloses well device converted timber, the acidylate wood fibre material of different appearance characteristics can once only be prepared out to the aceticacidanhydride high -usage, the utility model discloses ability reduction in production cost has fine industrialization prospect.
Description
Technical field
The utility model belongs to wood working and protection field, particularly relates to a kind of device simultaneously preparing the acetylize lignocellulosic material of different resemblance.
Background technology
Lignocellulosic material refers to the material mainly comprising the compositions such as Mierocrystalline cellulose, hemicellulose and xylogen in component, all contains great amount of hydroxy group in their structures, and hydrophilic ability is strong, easily absorbs water, and makes troubles thus to their application.As wooden unit, because it easily absorbs water, therefore easily expand with heat and contract with cold, cause wooden unit to be out of shape, ftracture, and easy breed bacteria; For wood powder and xylon, they are often processed to various types of materials, as wood is moulded together with resin; But because many, the hydrophilic abilities of hydroxyl in their structures are strong, therefore bad with resin compatible, and finally have impact on the performance of material.Given this; we need to carry out modification to lignocellulosic material; reduce hydroxyl quantity in its structure; reduce its water-absorbent; strengthen its germ resistance and and resin compatible, find that carrying out acetylize process to lignocellulosic material is a good solution (lignocellulosic material acetylization reaction process is as shown in Figure 1) by research.During lignocellulosic material generation acylation reaction, in its structure, hydroxyl is replaced by ethanoyl, and because ethanoyl does not have wetting ability, therefore after acylation modification, the wetting ability of lignocellulosic material and water-retaining capacity can reduce.Simultaneously; because ethanoyl volume is greater than hydrogen atom; so after acylation modification; duct in lignocellulosic material between cell walls and cell walls can block by large volume ethanoyl; so just more water molecules can be stoped to penetrate in lignocellulosic material, thus also can reduce the water-retaining capacity of lignocellulosic material more significantly.
Because ethanoyl molecular weight is greater than hydrogen, so its weight can increase after lignocellulosic material acetylize, conventional growth characterizes than (WPG), increases higher than larger explanation degree of acetylation.Increase and than (WPG) calculation formula be:
WPG＝(W2-W1)/W1×100％
Wherein, WPG is weightening finish ratio, and W2 is lignocellulosic material weight after acidylate, and W1 is lignocellulosic material weight before acidylate.
Acetylize lignocellulosic material is generally by carrying out reacting between lignocellulosic material and liquid acetic acid acid anhydride preparing; because liquid acetic acid acid anhydride easily penetrates into lignocellulosic material inside; inside and outside performance is consistent for the acidylate material of energy guarantee preparation, and this is particularly important to the lignocellulosic material preparing chunk.But when using liquid acetic acid acid anhydride and lignocellulosic material to react, the consumption of diacetyl oxide can be very large, can cause waste like this, reclaim the cost of diacetyl oxide after also increasing reaction simultaneously.Given this, people start again trial gas diacetyl oxide and lignocellulosic material reacts to prepare acetylize lignocellulosic material.First this way is heat liquid acetic acid acid anhydride, and make it seethe with excitement and produce gas diacetyl oxide, gas diacetyl oxide reacts with lignocellulosic material again.This method can save diacetyl oxide consumption, can reduce diacetyl oxide cost recovery, but gas diacetyl oxide permeates limited in lignocellulosic material, and therefore the method is only suitable for carrying out acidylate process to thin piece or film like, threadiness, Powdered lignocellulosic material.When needing to carry out acetylize process to the lignocellulosic material of various shapes feature simultaneously, just need to use at least two kinds of production equipments and production technique, troublesome poeration and cost is high.
Utility model content
The technical problems to be solved in the utility model is, overcomes deficiency of the prior art, provides a kind of device simultaneously preparing different resemblance acetylize lignocellulosic material.Utilize this device that liquid acetic acid acid anhydride and gas diacetyl oxide and different characteristics lignocellulosic material can be used to react simultaneously, complete the preparation of the acidylate lignocellulosic material of different resemblance simultaneously.
For technical solution problem, solution of the present utility model is:
A kind of device simultaneously preparing the acetylize lignocellulosic material of different resemblance is provided, comprises the first container as reactor; This device also comprises second container that can be airtight; Second container is arranged on the top of the first container, both internal space intercommunications, using the dividing plate laying multiple aperture as interval; Gas and liquid freely can pass through aperture, Powdered or fibrous lignocellulosic material then can be blocked not by; The sheathed heating unit of first outside of containers, sheathed collet outside second container.
In the utility model, described first container and second container have the side plate of integral type, and described dividing plate is movably arranged on the screens parts be located in the middle part of side plate inwall.
In the utility model, described first container and second container are splits; Described dividing plate is fixed on the bottom of second container, or active resting is placed in the upper limb of the first container side plate; The bottom of second container is movably arranged on the side plate upper limb of the first container by the mode clamped or spiral shell fills.
In the utility model, the top of described second container is provided with the removable cover that can seal.
In the utility model, described heating unit is oil bath heater, electric heater or microwave heater.
In the utility model, described dividing plate is the dividing plate of tetrafluoroethylene or polyvinylidene difluoride (PVDF) material.
By utilizing aforementioned means, the utility model can realize the acetylize lignocellulosic material simultaneously preparing different resemblance, and its concrete steps of the method comprise:
(1) lignocellulosic material of the bulk of thickness >=2mm, sheet or strip is placed in the first container, then adding liquid diacetyl oxide wherein, until lignocellulosic material is submerged;
(2) by film like, Powdered, fibrous lignocellulosic material, or the bulk of thickness < 2mm, sheet, strip lignocellulosic material be placed in second container;
(3) heating the first container makes liquid acetic acid acid anhydride seethe with excitement, the lignocellulosic material in the first container and liquid acetic acid acid anhydride generation acylation reaction; Meanwhile, the gas diacetyl oxide that boiling produces diffuses in second container by the aperture of dividing plate, with the lignocellulosic material generation acylation reaction in second container; Heating temperature 120 ~ 180 DEG C, 4 ~ 8 hours acylation reaction time;
(4) lignocellulosic material in two containers is taken out after acylation reaction; in the vacuum drying oven of 100 ~ 150 DEG C dry 4 ~ 12 hours respectively; remove unreacted diacetyl oxide and byproduct of reaction acetic acid, obtain the acetylize lignocellulosic material of different resemblance.
In the utility model, described lignocellulosic material refers in component the material comprising Mierocrystalline cellulose, hemicellulose and xylogen, and its source is any one in pine, China fir or maple.
In the utility model, before acylation reaction, by described lignocellulosic material heat drying to water content lower than 5%.
According to consumption, resemblance, the stacking mode of lignocellulosic material, and required acidylate degree is different, and the acylation reaction time of lignocellulosic material has different requirement.Because lignocellulosic material self also exists diversity, so its acidylate degree cannot realize controlling completely accurately.Operator can adjust the acidylate time according to practical situation, and after final acidylate, the WPG data of product are as the criterion whether met the demands.
Compared with prior art, the beneficial effects of the utility model are:
Diacetyl oxide utilization ratio in the utility model is high, can prepare the acidylate lignocellulosic material of different resemblance once; The utility model can reduce production cost, has good industrial prospect.
Accompanying drawing explanation
Fig. 1 is lignocellulosic material acetylization reaction process.
Fig. 2 is the structural representation of acetylization reaction device in the utility model.
Reference numeral in figure: the first container 1, second container 2, dividing plate 3, heating unit 4, collet 5.
Embodiment
Below in conjunction with accompanying drawing, specific implementation of the present utility model is described in detail.
Prepare the device of the acetylize lignocellulosic material of different resemblance simultaneously, comprise as the first container 1 of reactor second container 2 airtight with energy; Second container 2 is arranged on the top of the first container 1, both internal space intercommunications, and using the dividing plate 3 laying multiple aperture as interval, dividing plate can select tetrafluoroethylene or polyvinylidene difluoride (PVDF) material to make.Gas and liquid freely can pass through aperture, Powdered or fibrous lignocellulosic material then can be blocked not by; Sheathed heating unit 4 outside first container 1, heating unit 4 can be oil bath heater, electric heater or microwave heater.The top of second container 2 is provided with the removable cover that can seal, sheathed collet 5 outside it.
First container 1 and second container 2 have multiple mode of connection optional, and those skilled in the art can complete design or type selecting according to actual needs.Be exemplified below:
(1) first container 1 and second container 2 have the side plate of integral type, and dividing plate 3 is movably arranged on the screens parts be located in the middle part of side plate inwall.
(2) first containers 1 and second container 2 are splits; Dividing plate 3 is fixed on the bottom of second container 2, or active resting is placed in the upper limb of the first container 1 side plate; The bottom of second container 2 is movably arranged on the side plate upper limb of the first container 1 by the mode clamped or spiral shell fills.
Based on the use of said apparatus, the utility model can prepare the method for the acetylize lignocellulosic material of different resemblance simultaneously, and its concrete steps comprise:
(1) lignocellulosic material of the bulk of thickness >=2mm, sheet or strip is placed in the first container, then adding liquid diacetyl oxide wherein, until lignocellulosic material is submerged;
(2) by film like, Powdered, fibrous lignocellulosic material, or the bulk of thickness < 2mm, sheet, strip lignocellulosic material be placed in second container;
(3) heating the first container makes liquid acetic acid acid anhydride seethe with excitement, the lignocellulosic material in the first container and liquid acetic acid acid anhydride generation acylation reaction; Meanwhile, the gas diacetyl oxide that boiling produces diffuses in second container by the aperture of dividing plate, with the lignocellulosic material generation acylation reaction in second container; Heating temperature 120 ~ 180 DEG C, 4 ~ 8 hours acylation reaction time;
(4) lignocellulosic material in two containers is taken out after acylation reaction; in the vacuum drying oven of 100 ~ 150 DEG C dry 4 ~ 12 hours respectively; remove unreacted diacetyl oxide and byproduct of reaction acetic acid, obtain the acetylize lignocellulosic material of different resemblance.
Described lignocellulosic material refers in component the material comprising Mierocrystalline cellulose, hemicellulose and xylogen, and its source is any one in pine, China fir or maple.
Before acylation reaction, by described lignocellulosic material heat drying to water content lower than 5%.
Embodiment 1
Wood (length × wide × thick=100 × 50 × 2mm is loosened in first container 1, moisture < 5%), wood powder (particle diameter 50 ~ 100 order is loosened in second container 2, moisture≤3%), Heating temperature 120 DEG C in first container 1, reaction times 4h, reaction terminates rear pine 120 DEG C of vacuum drying ovens dryings 4 hours, and pine powder was 100 DEG C of vacuum drying ovens dryings 12 hours.After acidylate, WPG is respectively: pine 24%, pine powder 28% (note: timber was do not have WPG data before carrying out acidylate process).
Embodiment 2
Wood (length × wide × thick=100 × 50 × 2mm is loosened in first container 1, moisture < 5%), wood powder (particle diameter 50 ~ 100 order is loosened in second container 2, moisture≤3%), Heating temperature 180 DEG C in first container 1, reaction times 4h, reaction terminates rear pine 150 DEG C of vacuum drying ovens dryings 4 hours, and pine powder was 120 DEG C of vacuum drying ovens dryings 8 hours.After acidylate, WPG is respectively: pine 27%, pine powder 28%.
Embodiment 3
China fir (length × wide × thick=100 × 50 × 2.5mm is put in first container 1, moisture < 5%), fir powder (particle diameter 30 ~ 200 order is put in second container 2, moisture≤3%), Heating temperature 150 DEG C in first container 1, reaction times 4h, reaction terminates rear China fir 120 DEG C of vacuum drying ovens dryings 4 hours, and fir powder was 100 DEG C of vacuum drying ovens dryings 8 hours.After acidylate, WPG is respectively: China fir 25%, fir powder 28%.
Embodiment 4
China fir (length × wide × thick=100 × 50 × 3mm is put in first container 1, moisture < 5%), Chinese Fir for Fibre (length 1 ~ 5mm is put in second container 2, radical length 10-50 μm, moisture≤3%), Heating temperature 120 DEG C in the first container 1, reaction times 5h, reaction terminates rear China fir 150 DEG C of vacuum drying ovens dryings 10 hours, and Chinese Fir for Fibre was 120 DEG C of vacuum drying ovens dryings 4 hours.After acidylate, WPG is respectively: China fir 20%, Chinese Fir for Fibre 27%.
Embodiment 5
Maple (length × wide × thick=100 × 50 × 2mm is put in first container 1, moisture < 5%), maple powder (particle diameter 100 ~ 200 order is put in second container 2, moisture≤3%), Heating temperature 140 DEG C in first container 1, reaction times 6h, reaction terminates rear maple 120 DEG C of vacuum drying ovens dryings 8 hours, and maple powder was 150 DEG C of vacuum drying ovens dryings 4 hours.After acidylate, WPG is respectively: maple 22%, maple powder 28%.
Embodiment 6
Maple (length × wide × thick=100 × 50 × 5mm is put in first container 1, moisture < 5%), maple fibers (length 1 ~ 5mm is put in second container 2, radical length 10-50 μm, moisture≤3%), Heating temperature 160 DEG C in the first container 1, reaction times 5h, reaction terminates rear maple 150 DEG C of vacuum drying ovens dryings 12 hours, and maple fibers was 100 DEG C of vacuum drying ovens dryings 5 hours.After acidylate, WPG is respectively: maple 15%, maple fibers 28%.
Embodiment 7
Wood (length × wide × thick=100 × 50 × 2.5mm is loosened in first container 1, moisture < 5%), wood powder (particle diameter 30 ~ 100 order is separately loosened in second container 2, moisture≤3%) and maple fibers (length 1 ~ 5mm, radical length 10-50 μm, moisture≤3%), Heating temperature 150 DEG C in first container 1, reaction times 8h, reaction terminates rear pine 120 DEG C of vacuum drying ovens dryings 4 hours, and pine powder and maple fibers were 120 DEG C of vacuum drying ovens dryings 8 hours.After acidylate, WPG is respectively: pine 24%, pine powder 26%, maple fibers 27%.
Embodiment 8
China fir (length × wide × thick=100 × 50 × 4mm is put in first container 1, moisture < 5%), wood powder (particle diameter 30 ~ 100 order is separately loosened in second container 2, moisture≤3%) and maple fibers (length 1 ~ 5mm, radical length 10-50 μm, moisture≤3%), Heating temperature 180 DEG C in first container 1, reaction times 6h, reaction terminates rear pine 100 DEG C of vacuum drying ovens dryings 8 hours, and pine powder and maple fibers were 100 DEG C of vacuum drying ovens dryings 6 hours.After acidylate, WPG is respectively: China fir 20%, pine powder 26%, maple fibers 27%.
Embodiment 9
China fir (length × wide × thick=100 × 50 × 4mm is put in first container 1, moisture < 5%), China fir (length × wide × thick=100 × 50 × 1.5mm is put in second container 2, moisture < 5%), Heating temperature 150 DEG C in first container 1, reaction times 6h, reaction terminates latter two China fir 130 DEG C of vacuum drying ovens dryings 8 hours.After acidylate, WPG is respectively: China fir 22% in the first container 1, China fir 28% in second container 2.
Claims (6)
1. prepare the device of the acetylize lignocellulosic material of different resemblance simultaneously, comprise the first container as reactor; It is characterized in that, this device also comprises second container that can be airtight; Second container is arranged on the top of the first container, both internal space intercommunications, using the dividing plate laying multiple aperture as interval; Gas and liquid freely can pass through aperture, Powdered or fibrous lignocellulosic material then can be blocked not by; The sheathed heating unit of first outside of containers, sheathed collet outside second container.
2. device according to claim 1, is characterized in that, described first container and second container have the side plate of integral type, and described dividing plate is movably arranged on the screens parts be located in the middle part of side plate inwall.
3. device according to claim 1, is characterized in that, described first container and second container are splits; Described dividing plate is fixed on the bottom of second container, or active resting is placed in the upper limb of the first container side plate; The bottom of second container is movably arranged on the side plate upper limb of the first container by the mode clamped or spiral shell fills.
4. according to the device described in claims 1 to 3 any one, it is characterized in that, the top of described second container is provided with the removable cover that can seal.
5. according to the device described in claims 1 to 3 any one, it is characterized in that, described heating unit is oil bath heater, electric heater or microwave heater.
6. according to the device described in claims 1 to 3 any one, it is characterized in that, described dividing plate is the dividing plate of tetrafluoroethylene or polyvinylidene difluoride (PVDF) material.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520910163.3U CN205170723U (en) | 2015-11-15 | 2015-11-15 | Device of different appearance characteristic acetylation wood fibre materials of coproduction |
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| CN201520910163.3U CN205170723U (en) | 2015-11-15 | 2015-11-15 | Device of different appearance characteristic acetylation wood fibre materials of coproduction |
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| CN205170723U true CN205170723U (en) | 2016-04-20 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105348543A (en) * | 2015-11-15 | 2016-02-24 | 浙江大学自贡创新中心 | Device for simultaneously preparing acetylated wood fiber materials with different shape characters |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105348543A (en) * | 2015-11-15 | 2016-02-24 | 浙江大学自贡创新中心 | Device for simultaneously preparing acetylated wood fiber materials with different shape characters |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160420 Termination date: 20211115 |