CN102321396A - Process for depolymerizing and purifying high-performance and environment-friendly phenylalanine ammonia lyase (PAL) flame-retardant material - Google Patents
Process for depolymerizing and purifying high-performance and environment-friendly phenylalanine ammonia lyase (PAL) flame-retardant material Download PDFInfo
- Publication number
- CN102321396A CN102321396A CN201110149481A CN201110149481A CN102321396A CN 102321396 A CN102321396 A CN 102321396A CN 201110149481 A CN201110149481 A CN 201110149481A CN 201110149481 A CN201110149481 A CN 201110149481A CN 102321396 A CN102321396 A CN 102321396A
- Authority
- CN
- China
- Prior art keywords
- pal
- depolymerization
- purifying
- flame
- performance
- 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
- 239000000463 material Substances 0.000 title claims abstract description 116
- 239000003063 flame retardant Substances 0.000 title claims abstract description 44
- 238000000034 method Methods 0.000 title claims abstract description 38
- 230000008569 process Effects 0.000 title claims abstract description 19
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 title abstract description 17
- 108700023158 Phenylalanine ammonia-lyases Proteins 0.000 title abstract 6
- 230000009471 action Effects 0.000 claims abstract description 7
- 238000005516 engineering process Methods 0.000 claims description 15
- 239000002245 particle Substances 0.000 claims description 11
- 238000000746 purification Methods 0.000 claims description 7
- 230000005484 gravity Effects 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 26
- 229910001868 water Inorganic materials 0.000 abstract description 26
- 230000036571 hydration Effects 0.000 abstract description 23
- 238000006703 hydration reaction Methods 0.000 abstract description 23
- 239000012535 impurity Substances 0.000 abstract description 22
- 239000010410 layer Substances 0.000 abstract description 22
- 239000003814 drug Substances 0.000 abstract description 13
- 150000001768 cations Chemical class 0.000 abstract description 6
- 239000011229 interlayer Substances 0.000 abstract description 6
- 239000000843 powder Substances 0.000 abstract description 6
- 230000006378 damage Effects 0.000 abstract description 5
- 239000006185 dispersion Substances 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 5
- 230000008901 benefit Effects 0.000 abstract description 2
- 230000000887 hydrating effect Effects 0.000 abstract 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 14
- 239000011707 mineral Substances 0.000 description 14
- 238000009792 diffusion process Methods 0.000 description 11
- 239000012530 fluid Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 8
- 239000011159 matrix material Substances 0.000 description 8
- 230000008961 swelling Effects 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- 208000037656 Respiratory Sounds Diseases 0.000 description 4
- 229910052736 halogen Inorganic materials 0.000 description 4
- 150000002367 halogens Chemical class 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 229910052755 nonmetal Inorganic materials 0.000 description 4
- 230000006641 stabilisation Effects 0.000 description 4
- 238000011105 stabilization Methods 0.000 description 4
- 230000002522 swelling effect Effects 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 238000005188 flotation Methods 0.000 description 3
- 239000002105 nanoparticle Substances 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 238000009736 wetting Methods 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- 208000035126 Facies Diseases 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 229910001919 chlorite Inorganic materials 0.000 description 2
- 229910052619 chlorite group Inorganic materials 0.000 description 2
- QBWCMBCROVPCKQ-UHFFFAOYSA-N chlorous acid Chemical compound OCl=O QBWCMBCROVPCKQ-UHFFFAOYSA-N 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000006355 external stress Effects 0.000 description 2
- 239000010433 feldspar Substances 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 229910052900 illite Inorganic materials 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002086 nanomaterial Substances 0.000 description 2
- 239000011858 nanopowder Substances 0.000 description 2
- VGIBGUSAECPPNB-UHFFFAOYSA-L nonaaluminum;magnesium;tripotassium;1,3-dioxido-2,4,5-trioxa-1,3-disilabicyclo[1.1.1]pentane;iron(2+);oxygen(2-);fluoride;hydroxide Chemical compound [OH-].[O-2].[O-2].[O-2].[O-2].[O-2].[F-].[Mg+2].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[K+].[K+].[K+].[Fe+2].O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2 VGIBGUSAECPPNB-UHFFFAOYSA-L 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000001846 repelling effect Effects 0.000 description 2
- 230000000979 retarding effect Effects 0.000 description 2
- 235000019600 saltiness Nutrition 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 150000004760 silicates Chemical class 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 238000005728 strengthening Methods 0.000 description 2
- 230000035882 stress Effects 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- JYEUMXHLPRZUAT-UHFFFAOYSA-N 1,2,3-triazine Chemical compound C1=CN=NN=C1 JYEUMXHLPRZUAT-UHFFFAOYSA-N 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000282414 Homo sapiens Species 0.000 description 1
- 229910019092 Mg-O Inorganic materials 0.000 description 1
- 229910019395 Mg—O Inorganic materials 0.000 description 1
- 229910014142 Na—O Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910018557 Si O Inorganic materials 0.000 description 1
- 238000005411 Van der Waals force Methods 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- GANNOFFDYMSBSZ-UHFFFAOYSA-N [AlH3].[Mg] Chemical compound [AlH3].[Mg] GANNOFFDYMSBSZ-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 229910001850 copernicium Inorganic materials 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000008396 flotation agent Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 238000009830 intercalation Methods 0.000 description 1
- 230000002687 intercalation Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000002114 nanocomposite Substances 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Inorganic materials [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The invention relates to the technical field of flame-retardant materials, in particular to a process for depolymerizing and purifying a high-performance and environment-friendly phenylalanine ammonia lyase (PAL) flame-retardant material, and solves the technical problems that the prior art is unreasonable and the like. The process comprises the following steps of: A, depolymerizing; and B, purifying. Compared with the prior art, the process for depolymerizing and purifying the high-performance and environment-friendly PAL flame-retardant material has the advantages that: the dynamic action of hydration expansive force generated by hydration of a high-speed water medium and a substance and repulsive force of a diffused electric double layer formed by fully hydrating interlayer cations is fully exerted, disintegration and dispersion are promoted, the material is separated from impurities and purified (the medium water can be recycled), chemical impurities are prevented from being introduced and environment pollution harm is avoided in the conventional medicament floatation, high-purity micro/nano PAL material powder is prepared, and a material basis is provided for preparing the high-performance and environment-friendly flame-retardant material.
Description
Technical field
The present invention relates to the fire retardant material technical field, especially relate to a kind of high-performance environment protection type PAL fire retardant material depolymerization purifying technique.
Background technology
Fire-retardant essential for human beings'health and safety, The development in society and economy, its significance is self-evident.In self the fire-fighting demand in fields such as building, chemical industry, military affairs and traffic and the field of tool inflammableness macromolecular material, fire retardant material is reducing ratio aspect the fire hazard up to more than 70%.Facts have proved that fire retardant material is avoided heavy economic losses and the aspect of preserving the ecological environment reducing the fire loss of life and personal injury; All bring into play big emphatically effect; Thereby, the research of fire retardant and fire retardant material, production and application, significant for socio-economic development " mankind and environment ".At present, common fire retardant mainly contains halogenated flame retardant, silicon-series five-retardant, phosphorus flame retardant, triazine flame retardant and inorganic combustion inhibitor.China is main with halogen containing flame-retardants such as bromine system, chlorine systems; Though the Halogen fire retardant material has good flame-retardant effect; But can discharge a large amount of smog and poisonous, harmful corrosive gases during general Halogen fire retardant material presence of fire, personnel and precision instrument are brought very big infringement.Strictness along with the global environment rules; China requires the reinforcement of dynamics to flame-retarded technology; People require increasingly high to fire safety and goods fire-retardant, Halogen, low cigarette, low toxicity, high-performance environment protection type flame-proof agent have become the target of socio-economic development and the harmonious pursuit of environment.
The PAL material is the green flame retardant of excellent performance, disturbs intercalation, peel ply, the chain flame retarding construction function of supporting component of combustion but have, and contains multiple ignition-proof element (Si, P, S, B) and press down cigarette element (Mo, Fe, Mg, Zn, Cn).The structure construction of PAL material is the structure of layer, chain, fibrous crystalline structure and nano level hole passage.It is an oblique system, and crystalline structure belongs to 2:1 type non-metallic minerals, promptly two-layer silicon-oxy tetrahedron folder one deck magnesium (aluminium) octahedron, and its tetrahedron and octahedral arrangement mode are laminate structure.In each 2:1 layer, the tetrahedron corner is pushed up at a certain distance direction and is put upside down form layers, chain combination characteristic.Form parallel at tetrahedron bar interband with chain; The passage that runs through skeleton; Channel cross-section is about 0.37nm * 0.63nm; Passage is that water molecules is filled, for the zeolite water (H2O) that is parallel to fiber and with mg ion coordinate crystal water (OH2), have surface adsorption water (H2O) and with octahedral cations coordinate water of constitution (OH).Its crystalline structure is a needle-like, is made up of elongated hollow tube.The unevenness on PAL material surface micromorphology performance structure surface rises and falls, and especially cleavage surface is very coarse, has the step of 1-2nm to occur, and presents the complicated micromorphology of distortion and spiral.Parallel fibers tunnel hole accounts for more than 1/2 of fiber volume, and interior external surface area is considerable, and the duct effect is remarkable.Combine with molecular linkage between the PAL material layer, even K+, Na+ are arranged, K-O, also much smaller than the linkage force of Si-O or Mg-O, water molecules, atoms metal, organic molecule can get into interlayer to the bonding force of Na-O key, make interfloor distance (interlamination region) that mutability arranged.The PAL material has unique layer, chain crystalline structure, has given PAL material particular performances.
Natural nano-mineral adsorbs each other usually or inlays, and is polymer state output, also is mixed with different quantities impurity, thereby the mineral material nano effect can't be brought into play.And inorganic fire-retarded the material that uses mostly at present is generally micron order, and fire-retardant loading level is big, and flame retarding efficiency is not high, and the problem of caused technology and product performance all compares seriously.Its mechanism reason is that micro materials can't realize that nanoparticle forms the structure and the form of nano composite material in polymeric matrix, and directly affect matrix material fire-retardant, strengthen overall performance such as mechanical characteristic.The more important thing is and affect and the consistency of polymeric matrix and the dispersiveness in polymeric matrix.Uses at present usually employing chemical flotation agent (medicament) or disperse as media implementation with non-aqueous solution.Above any way has all been introduced chemical, brings new impurity into for product (raw material), and environment is caused new pollution, need take disposal technology technology and increase input.
Summary of the invention
The objective of the invention is provides a kind of polymerization that can break between high-purity PAL material to the problems referred to above, makes it to form dispersive nanometer or submicron monomer, and can not cause the high-performance environment protection type PAL fire retardant material depolymerization purifying technique of environmental pollution.
For achieving the above object, the present invention has adopted following technical proposal: this high-performance environment protection type PAL fire retardant material depolymerization purifying technique is characterized in that this technology comprises the steps:
A, depolymerization: adopt target plate formula flow kibbler to carry out depolymerization and disperse; Be that medium carries high-purity PAL material promptly, bump against that material and target plate are in high velocity impact, bump with the fixedly target plate that is provided with the high speed flow; The high-speed functions of flow finally changes the crushing energy of material into, makes material broken;
B, purification: adopt the screw propulsion whizzer to realize purifying; Promptly in screw centrifuge screw rod propelled at high velocity process; Utilize the action of gravity of material particles size; Spiral separates the material of different-grain diameter, and control depolymerization dispersive paste consistency, front end can obtain from the subparticle of the different-grain diameter of<100nm-10 μ m.
Mix in the PAL material feedstock impurity such as chlorite, illite, feldspar and carbonate are arranged; Fully compatiblely in matrix also need the PAL material of certain purity and micro/nano level with homodisperse, thus need disperse through depolymerization, warp separates with impurity and the technical matters of purifying prepares high-purity PAL material.In addition, though the PAL material is natural nonmetal nano-mineral, the nanoparticle material property is arranged; But owing to there is interfloor distance (interlamination region), characteristics of particles and interlamination region structure are prone to be polymer; Thereby need be through depolymerization; And it is fully dissociated and high dispersing in medium, could realize that the consistency in the polymeric matrix is good, dispersed height, thereby strengthen overall performances such as it is fire-retardant, mechanical characteristic.Therefore, the stabilization stabilization of purifying and Depolymerization Technique and technology, the optimization of flow process is to guarantee the layered nano PAL flame-retardant material flame retardant properties and realize the basis of industrialization, most important technical matters.
What the micro-nano powder technology of preparing was advanced is high speed flow ability method, and it is divided into air-flow and two kinds of forms of flow.With regard to high speed flow ability method, flow is pulverized has the fineness higher than comminution by gas stream, for very difficult some the micro-nano material realized in the comminution by gas stream field of force, serves as when pulverizing the field of force, then might realize micro-nanoization with flow power.In addition, serve as to pulverize in the process in the field of force with flow power, can avoid static, spark and partial temperature too high, thereby crushing process is comparatively safe.Fluid medium has good immersional wetting to material, can significantly reduce the particulate surface energy, reduces the required stress that ruptures; And from the process of particle fracture, according to the crack propagation condition, the fluid medium molecular adsorption can reduce the required external stress of crack propagation at fresh surface, promotes the expansion of crackle, and prevents the closed again of newborn crackle.If water medium; The aquation of material and water (water-swelling) effect reduces material grains volumetric expansion, hardness, reduces depolymerization and disperses required surging force; The positively charged ion aquation break away to form diffusion double layer and strengthens depolymerization and disperse between the particle nanometer layer, realization and separate impurities and obtain purification.The adding of medicament, the generation foam breaks and has encircled hydration and positively charged ion diffusion double layer, therefore, except that introducing impurity and damaging the environment, has checked depolymerization, the reduction dispersion effect of material grains on the contrary, and the purpose that separation is purified is difficult to realize.The present invention makes full use of the PAL material in water medium camber dispersive natural endowment property characteristics, and employing water is that fluid medium, no medicament add, and integrates flow process reasonableness, non-secondary pollution and resources circulation economy characteristic in one, prepares high-purity PAL material.
The raw material of PAL material is the sedimentary natural nonmetal silicates mineral of marine facies (semiclosed salty lake), is polar material, meets water the hydration swelling effect can take place, and gets into formation diffusion double layer in back in the water, further expands, and makes the mineral volume increase 8-20 doubly.Hydration weakens and has destroyed intergranular connection; Make particle along existing combination vulnerable area (like the set face of uncracked bedding, schistosity, wall reason, mineral grain and the mineral face etc. that dissociates); Form new crack; Make grain breakage, reduce the particulate mechanical strength, pulverize for further flow and reduced energy consumption.
Technical matters based on high-purity fully, the fine PAL material of the high speed flow legal system powder of the no medicament of ydrodynamics principle; Because the hydration swelling that the hydration of high speed flow and material produces and two electric depolymerization power of repelling; Height of materials is disperseed, accomplish miniaturization.Utilize differently, realize separating and purifying with impurity through the spiral centrifugal device with the gravity of impurity.Technological process of the present invention does not have waste gas, discharge of wastewater, and waste residue can be processed as agricultural siliceous fertilizer and macromolecular material strengthening agent WHITE CARBON BLACK, has realized that " environmentally friendly ", resource utilization are close to 100% " resources conservation ".
The present invention uses no medicament high speed flow law technology and depolymerization dispersion and the purification separating technology based on the ydrodynamics principle; The hydration swelling power of having given full play to the hydration of high speed water medium and material and having produced; The dynamic action of the diffusion double layer repulsive force that forms with the abundant aquation of interlayer cation; Promote to disintegrate disperse, separate with impurity and realize purifying (WATER AS FLOW MEDIUM reusable edible), avoided traditional medicament flotation to introduce the harm of impurity atom and contaminate environment; Formulate out high-purity, micro-nano PAL material powder, for manufacturing high-performance, environmental protection flame retardant material provide material foundation.
In above-mentioned high-performance environment protection type PAL fire retardant material depolymerization purifying technique, in above-mentioned steps A, the paste consistency after depolymerization disperses is 15%-20%.
In above-mentioned high-performance environment protection type PAL fire retardant material depolymerization purifying technique, in above-mentioned step B, the rotating speed of screw centrifuge is controlled at 1500r/min-2500r/min.
In above-mentioned high-performance environment protection type PAL fire retardant material depolymerization purifying technique, the PAL material content in described high-purity PAL material is 90%-98%.
Compared with prior art; The advantage of this high-performance environment protection type PAL fire retardant material depolymerization purifying technique is: given full play to the hydration of high speed water medium and material and the dynamic action of the diffusion double layer repulsive force that the abundant aquation of the hydration swelling power that produces and interlayer cation forms; Promote to disintegrate and disperse; Separate and realize purifying (WATER AS FLOW MEDIUM reusable edible) with impurity; Avoided traditional medicament flotation to introduce the harm of impurity atom and contaminate environment, formulated out high-purity, micro-nano PAL material powder, for manufacturing high-performance, environmental protection flame retardant material provide material foundation.
Embodiment
This high-performance environment protection type PAL fire retardant material depolymerization purifying technique comprises the steps:
A, depolymerization: adopt target plate formula flow kibbler to carry out depolymerization and disperse; Be that medium carries high-purity PAL material promptly, bump against that material and target plate are in high velocity impact, bump with the fixedly target plate that is provided with the high speed flow; The high-speed functions of flow finally changes the crushing energy of material into, makes material broken.Paste consistency after depolymerization disperses is 15%-20%.PAL material content in described high-purity PAL material is 90%-98%.
B, purification: adopt the screw propulsion whizzer to realize purifying; Promptly in screw centrifuge screw rod propelled at high velocity process; Utilize the action of gravity of material particles size; Spiral separates the material of different-grain diameter, and control depolymerization dispersive paste consistency obtains the subparticle less than the different-grain diameter of 100nm-10 μ m.The rotating speed of screw centrifuge is controlled at 1500r/min-2500r/min.
Mix in the PAL material feedstock impurity such as chlorite, illite, feldspar and carbonate are arranged; Fully compatiblely in matrix also need the PAL material of certain purity and micro/nano level with homodisperse, thus need disperse through depolymerization, warp separates with impurity and the technical matters of purifying prepares high-purity PAL material.In addition, though the PAL material is natural nonmetal nano-mineral, the nanoparticle material property is arranged; But owing to there is interfloor distance (interlamination region), characteristics of particles and interlamination region structure are prone to be polymer; Thereby need be through depolymerization; And it is fully dissociated and high dispersing in medium, could realize that the consistency in the polymeric matrix is good, dispersed height, thereby strengthen overall performances such as it is fire-retardant, mechanical characteristic.Therefore, the stabilization stabilization of purifying and Depolymerization Technique and technology, the optimization of flow process is to guarantee the layered nano PAL flame-retardant material flame retardant properties and realize the basis of industrialization, most important technical matters.
What the micro-nano powder technology of preparing was advanced is high speed flow ability method, and it is divided into air-flow and two kinds of forms of flow.With regard to high speed flow ability method, flow is pulverized has the fineness higher than comminution by gas stream, for very difficult some the micro-nano material realized in the comminution by gas stream field of force, serves as when pulverizing the field of force, then might realize micro-nanoization with flow power.In addition, serve as to pulverize in the process in the field of force with flow power, can avoid static, spark and partial temperature too high, thereby crushing process is comparatively safe.Fluid medium has good immersional wetting to material, can significantly reduce the particulate surface energy, reduces the required stress that ruptures; And from the process of particle fracture, according to the crack propagation condition, the fluid medium molecular adsorption can reduce the required external stress of crack propagation at fresh surface, promotes the expansion of crackle, and prevents the closed again of newborn crackle.If water medium; The aquation of material and water (water-swelling) effect reduces material grains volumetric expansion, hardness, reduces depolymerization and disperses required surging force; The positively charged ion aquation break away to form diffusion double layer and strengthens depolymerization and disperse between the particle nanometer layer, realization and separate impurities and obtain purification.The adding of medicament, the generation foam breaks and has encircled hydration and positively charged ion diffusion double layer, therefore, except that introducing impurity and damaging the environment, has checked depolymerization, the reduction dispersion effect of material grains on the contrary, and the purpose that separation is purified is difficult to realize.The present invention makes full use of the PAL material in water medium camber dispersive natural endowment property characteristics, and employing water is that fluid medium, no medicament add, and integrates flow process reasonableness, non-secondary pollution and resources circulation economy characteristic in one, prepares high-purity PAL material.
The raw material of PAL material is the sedimentary natural nonmetal silicates mineral of marine facies (semiclosed salty lake), is polar material, meets water the hydration swelling effect can take place, and gets into formation diffusion double layer in back in the water, further expands, and makes the mineral volume increase 8-20 doubly.Hydration weakens and has destroyed intergranular connection; Make particle along existing combination vulnerable area (like the set face of uncracked bedding, schistosity, wall reason, mineral grain and the mineral face etc. that dissociates); Form new crack; Make grain breakage, reduce the particulate mechanical strength, pulverize for further flow and reduced energy consumption.
Huge the surface hydration ability and the swelling pressure show that the wettability that the PAL material is good (polarity) makes the hydration of fluid medium be able to give full play to.In addition, between PAL material crystal layer more weak Van der Waals force is only arranged, the aquation of these mineral that are not enough to contend with can, therefore, aquation can take place in PAL material crystal layer and outside surface, the suction of PAL material is prone to expand, legibility leaves under fluid medium.The aquation of compensating cation can (big more, hydroexpansivity is strong more), diffusion double layer thickness (diffusion double layer is thick more, hydration swelling property strong more), (pH value is high more, and surface potential is big more, the enhancing of hydration swelling property for the saltiness of fluid medium pH value; Saltiness is big, and hydration weakens), these factors also affect the aquation disassociation.The wetting ability of PAL material, high aquation can, the high pH value of weak interlayer power and 7.8-9.3, it is disperseed at the fluid medium camber, be to be convenient to depolymerization disperse and separates the natural endowment property characteristic of purifying with basic.
Technical matters based on high-purity fully, the fine PAL material of the high speed flow legal system powder of the no medicament of ydrodynamics principle; Because the hydration swelling that the hydration of high speed flow and material produces and two electric depolymerization power of repelling; Height of materials is disperseed, accomplish miniaturization.Utilize differently, realize separating and purifying with impurity through the spiral centrifugal device with the gravity of impurity.Technological process of the present invention does not have waste gas, discharge of wastewater, and waste residue can be processed as agricultural siliceous fertilizer and macromolecular material strengthening agent WHITE CARBON BLACK, has realized that " environmentally friendly ", resource utilization are close to 100% " resources conservation ".
The present invention uses no medicament high speed flow law technology and depolymerization dispersion and the purification separating technology based on the ydrodynamics principle; The hydration swelling power of having given full play to the hydration of high speed water medium and material and having produced; The dynamic action of the diffusion double layer repulsive force that forms with the abundant aquation of interlayer cation; Promote to disintegrate disperse, separate with impurity and realize purifying (WATER AS FLOW MEDIUM reusable edible), avoided traditional medicament flotation to introduce the harm of impurity atom and contaminate environment; Formulate out high-purity, micro-nano PAL material powder, for manufacturing high-performance, environmental protection flame retardant material provide material foundation.
Specific embodiment described herein only is that the present invention's spirit is illustrated.Person of ordinary skill in the field of the present invention can make various modifications or replenishes or adopt similar mode to substitute described specific embodiment, but can't depart from spirit of the present invention or surmount the defined scope of appended claims.
Although this paper has used term morely, do not get rid of the possibility of using other term.Using these terms only is in order to describe and explain essence of the present invention more easily; It all is contrary with spirit of the present invention being construed to any additional restriction to them.
Claims (4)
1. a high-performance environment protection type PAL fire retardant material depolymerization purifying technique is characterized in that this technology comprises the steps:
A, depolymerization: adopt target plate formula flow kibbler to carry out depolymerization and disperse; Be that medium carries high-purity PAL material promptly, bump against that material and target plate are in high velocity impact, bump with the fixedly target plate that is provided with the high speed flow; The high-speed functions of flow finally changes the crushing energy of material into, makes material broken;
B, purification: adopt the screw propulsion whizzer to realize purifying; Promptly in screw centrifuge screw rod propelled at high velocity process; Utilize the action of gravity of material particles size; Spiral separates the material of different-grain diameter, and control depolymerization dispersive paste consistency obtains the subparticle less than the different-grain diameter of 100nm-10 μ m.
2. high-performance environment protection type PAL fire retardant material depolymerization purifying technique according to claim 1 is characterized in that, in above-mentioned steps A, the paste consistency after depolymerization disperses is 15%-20%.
3. high-performance environment protection type PAL fire retardant material depolymerization purifying technique according to claim 1 is characterized in that in above-mentioned step B, the rotating speed of screw centrifuge is controlled at 1500r/min-2500r/min.
4. according to claim 1 or 2 or 3 described high-performance environment protection type PAL fire retardant material depolymerization purifying techniques, it is characterized in that the PAL material content in described high-purity PAL material is 90%-98%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201110149481A CN102321396A (en) | 2011-06-02 | 2011-06-02 | Process for depolymerizing and purifying high-performance and environment-friendly phenylalanine ammonia lyase (PAL) flame-retardant material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201110149481A CN102321396A (en) | 2011-06-02 | 2011-06-02 | Process for depolymerizing and purifying high-performance and environment-friendly phenylalanine ammonia lyase (PAL) flame-retardant material |
Publications (1)
Publication Number | Publication Date |
---|---|
CN102321396A true CN102321396A (en) | 2012-01-18 |
Family
ID=45449236
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201110149481A Pending CN102321396A (en) | 2011-06-02 | 2011-06-02 | Process for depolymerizing and purifying high-performance and environment-friendly phenylalanine ammonia lyase (PAL) flame-retardant material |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102321396A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103641126A (en) * | 2013-12-11 | 2014-03-19 | 甘肃金宇生态环境工程有限公司 | Method for preparing high-performance PAL (phenylalanine ammonia lyase) material by using non-metallic mineral palygorskite |
CN103783262A (en) * | 2013-12-11 | 2014-05-14 | 甘肃金宇生态环境工程有限公司 | Method for preparing safe and green natural forage material in culture industry |
CN111592892A (en) * | 2020-04-28 | 2020-08-28 | 山东科技大学 | Method for preparing high-performance PAL material by using non-metallic mineral palygorskite |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1439451A (en) * | 2002-11-18 | 2003-09-03 | 长沙矿冶研究院 | Nano-diamond deagglomeration and grading method |
CN101182203A (en) * | 2007-11-27 | 2008-05-21 | 山东大学 | Barium titanate-based piezoelectric ceramic material and its preparation method and application |
CN101643210A (en) * | 2009-06-29 | 2010-02-10 | 金堆城钼业股份有限公司 | Method for preparing ultrafine carbide powder |
CN101870871A (en) * | 2010-04-23 | 2010-10-27 | 杭州贝洋科技有限公司 | Preparation method for novel layered nano PAL flame-retardant material |
-
2011
- 2011-06-02 CN CN201110149481A patent/CN102321396A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1439451A (en) * | 2002-11-18 | 2003-09-03 | 长沙矿冶研究院 | Nano-diamond deagglomeration and grading method |
CN101182203A (en) * | 2007-11-27 | 2008-05-21 | 山东大学 | Barium titanate-based piezoelectric ceramic material and its preparation method and application |
CN101643210A (en) * | 2009-06-29 | 2010-02-10 | 金堆城钼业股份有限公司 | Method for preparing ultrafine carbide powder |
CN101870871A (en) * | 2010-04-23 | 2010-10-27 | 杭州贝洋科技有限公司 | Preparation method for novel layered nano PAL flame-retardant material |
Non-Patent Citations (1)
Title |
---|
卞景娟: "超细粉体设备的原理及分类", 《机电信息》 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103641126A (en) * | 2013-12-11 | 2014-03-19 | 甘肃金宇生态环境工程有限公司 | Method for preparing high-performance PAL (phenylalanine ammonia lyase) material by using non-metallic mineral palygorskite |
CN103783262A (en) * | 2013-12-11 | 2014-05-14 | 甘肃金宇生态环境工程有限公司 | Method for preparing safe and green natural forage material in culture industry |
CN111592892A (en) * | 2020-04-28 | 2020-08-28 | 山东科技大学 | Method for preparing high-performance PAL material by using non-metallic mineral palygorskite |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP3740318B1 (en) | Mechanochemical process for producing valuable products free from persistent organic pollutants and other organohalogen compounds from waste comprising plastics and plastic laminates | |
CN106902930B (en) | A sludge biological cell wall breaking device and method for the sludge biological cell wall breaking | |
CN110540397B (en) | Anti-cracking energy-saving heat-insulating aerated concrete block and preparation method thereof | |
CN102383179B (en) | A kind of method that industrial waste acid and phosphogypsum fully utilize | |
CN100510003C (en) | Preparation process of nano concave soil base inorganic flame-retarded agent | |
CN102321397A (en) | Preparation process for high-performance environmentally-friendly PAL (Phenylalanine Ammonia-Lyase) flame-retardant material | |
CN103084152A (en) | Treatment method for effectively improving microstructures and absorption properties of attapulgite and kieselguhr | |
CN102321396A (en) | Process for depolymerizing and purifying high-performance and environment-friendly phenylalanine ammonia lyase (PAL) flame-retardant material | |
CN105597697A (en) | Bamboo charcoal and montmorillonoid composite adsorbent and preparation method thereof | |
WO2023130790A1 (en) | Method for full resource utilization of graphite ores | |
CN101555111A (en) | Highly active activated cement grinding reinforcing agent and preparation process thereof | |
CN109233377B (en) | Nano toughened inorganic transparent protective coating | |
CN108328981B (en) | Method for preparing sintering-free self-insulation brick from sludge, mineralized refuse and construction refuse | |
CN103194172A (en) | Non-asbestos composite fiber and preparation method thereof | |
CN103274753B (en) | Red mud compound type foaming agent | |
CN102863254B (en) | Nano-particle material and preparation method thereof | |
CN104475260A (en) | Flotation system and method for separating ABS (Acrylonitrile Butadiene Styrene) and HIPS (High Impact Polystyrene) | |
CN102352136A (en) | Inorganic activation process of nanometer or submicron PAL material | |
CN104689794B (en) | A kind of sodium lauryl sulphate modification sand adsorbing material and preparation method thereof | |
CN105670059B (en) | Calcium silicate slag and calcium silicate slag base gum filler and preparation method thereof | |
CN114716174B (en) | Waste concrete active slag powder and preparation method and application thereof | |
CN115025756B (en) | A kind of preparation method of modified coal gangue adsorbent | |
CN113426941B (en) | Grinding-aid synergist for casting bentonite and preparation method thereof | |
CN102796321B (en) | Production method of PP nucleation reinforcement composition | |
CN115057649A (en) | Concrete expansion toughening anti-cracking agent and preparation method thereof |
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: 20120118 |