CN204448254U - A kind of mineral fibres deslagging device - Google Patents
A kind of mineral fibres deslagging device Download PDFInfo
- Publication number
- CN204448254U CN204448254U CN201520062324.8U CN201520062324U CN204448254U CN 204448254 U CN204448254 U CN 204448254U CN 201520062324 U CN201520062324 U CN 201520062324U CN 204448254 U CN204448254 U CN 204448254U
- Authority
- CN
- China
- Prior art keywords
- detritus tank
- liquid back
- back pipe
- communicated
- stirring vane
- 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.)
- Active
Links
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
The utility model discloses a kind of mineral fibres deslagging device, it relates to inorganic mineral fiber slagging-off field of mechanical technique, hydraulic fracture machine or disc mill are communicated with the one-level magma entrance of the first detritus tank, the first stirring vane is provided with in first detritus tank, first below of removing cinder notch is communicated with the top of the first liquid back pipe and the top of the first liquid back pipe is provided with the first screen cloth, the secondary magma outlet of the first detritus tank is communicated with the secondary magma magma entrance of the second detritus tank by pipeline, second stirring vane is provided with hairbrush, filter is located at the below of hairbrush and the two contact, the bottom of the second detritus tank is provided with second except cinder notch, second below of removing cinder notch is communicated with the top of the second liquid back pipe and the top of the second liquid back pipe is provided with the second screen cloth, first liquid back pipe is all communicated with hydraulic fracture machine or disc mill by main pipe rail with the other end of the second liquid back pipe, the utility model is easy to use, easy and simple to handle, saves time, and increases work efficiency.
Description
Technical field:
The utility model relates to a kind of mineral fibres deslagging device, belongs to inorganic mineral fiber slagging-off field of mechanical technique.
Background technology:
Inorganic mineral fiber, usually by the winding-up of the raw mineral materials of molten state or to get rid of silk shaping, by usually comprising the particulate material of a large amount of non-fibroblast in the inorfil of this explained hereafter, is commonly referred to slag ball.Loosely, other are then tightr for the contact gear ratio of part slag ball and cellucotton.In slag ball more than diameter 0.25mm be called as thick slag ball, below diameter 0.25mm is called as thin slag ball.The existence of slag ball has great adverse effect to the mechanical performance of fibre and heat-proof quality, therefore in the production technology of various inorganic mineral fiber product, nearly all contains deslagging process to remove the slag ball comprised in raw material.
Due to slag ball and mineral fibres density difference very little, the free-falling velocity difference of both general in separating medium is separated, and according to the difference of separating medium, the deslagging process of mineral fibres can be divided into dry and wet way two class.
Dry method take air as separating medium, procedure of fibre production business usually uses dry method simply to remove the gred work before product export, effectively can remove the thick slag ball of the loose combination with cellucotton, but to thin slag ball and and cellucotton compact slag ball separating effect very poor.
Wet method is with liquid such as water for separating medium, and because the density of liquid is much larger than air, the density contrast of slag ball and separating medium is relatively little, and separation accuracy is higher.Chinese patent CN202305357U devises a kind of slag ball content meter, and it carries out flotation by changing flow velocity, need iterative cycles to carry out slagging-off work, but efficiency is too low, is applied to industrial production after being not suitable for amplification for obtaining higher slag ball yield.Chinese patent CN203264875U discloses a kind of slag removal equipment for glass fibre, and its essence is hydrocyclone, better to heterogeneous granular separating effects such as the iron filings in slurries, but not high to the separating power of slag ball.Some other box scummer or multistage fiber deslagging facility, owing to lacking efficient dispersion means, can not by with the compact slag ball of cellucotton and fiber separation, slagging-off effect still undesirable.In addition, because the free-falling velocity difference of thin slag ball and mineral fibres is very little, above process is all difficult to it to be effectively separated.
Utility model content:
For the problems referred to above, the technical problems to be solved in the utility model is to provide a kind of mineral fibres deslagging device.
The utility model comprises hydraulic fracture machine or disc mill, first detritus tank, second detritus tank, first stirring vane, second stirring vane, first screen cloth, second screen cloth, first liquid back pipe, second liquid back pipe, filter, hairbrush, hydraulic fracture machine or disc mill are communicated with the one-level magma entrance of the first detritus tank by pipeline, the first stirring vane is provided with in first detritus tank, the bottom of the first detritus tank is provided with first except cinder notch, first below of removing cinder notch is communicated with the top of the first liquid back pipe and the top of the first liquid back pipe is provided with the first screen cloth, the secondary magma outlet of the first detritus tank is communicated with the secondary magma magma entrance of the second detritus tank by pipeline, the second stirring vane and filter is provided with in second detritus tank, second stirring vane is provided with hairbrush, filter is located at the below of hairbrush and the two contact, the bottom of the second detritus tank is provided with second except cinder notch, second below of removing cinder notch is communicated with the top of the second liquid back pipe and the top of the second liquid back pipe is provided with the second screen cloth, first liquid back pipe is all communicated with hydraulic fracture machine or disc mill by main pipe rail with the other end of the second liquid back pipe, second detritus tank is provided with the outlet of good slurry.
The beneficial effects of the utility model are: this device utilizes hydrabrusher or disc mill to carry out high efficiency dispersion to mineral fibres, afterwards by two multistage detritus tank slagging-off, compared with prior art, device is simple, slag ball yield is high, effectively can be separated combine closely slag ball on cellucotton and the minimum thin slag ball of particle diameter.
Accompanying drawing illustrates:
For ease of illustrating, the utility model is described in detail by following concrete enforcement and accompanying drawing.
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention:
For making the purpose of this utility model, technical scheme and advantage clearly understand, below by the specific embodiment shown in accompanying drawing, the utility model is described.But should be appreciated that, these describe just exemplary, and do not really want to limit scope of the present utility model.In addition, in the following description, the description to known features and technology is eliminated, to avoid unnecessarily obscuring concept of the present utility model.
As shown in Figure 1, this detailed description of the invention is by the following technical solutions: it comprises hydraulic fracture machine or disc mill 1, first detritus tank 2, second detritus tank 3, first stirring vane 4, second stirring vane 5, first screen cloth 6, second screen cloth 7, first liquid back pipe 8, second liquid back pipe 9, filter 10, hairbrush 11, hydraulic fracture machine or disc mill 1 are communicated with the one-level magma entrance 21 of the first detritus tank 2 by pipeline, the first stirring vane 4 is provided with in first detritus tank 2, the bottom of the first detritus tank 2 is provided with first except cinder notch 22, first below of removing cinder notch 22 is communicated with the top of the first liquid back pipe 8 and the top of the first liquid back pipe 8 is provided with the first screen cloth 6, the secondary magma outlet 23 of the first detritus tank 2 is communicated with the secondary magma magma entrance 31 of the second detritus tank 3 by pipeline, the second stirring vane 5 and filter 10 is provided with in second detritus tank 3, second stirring vane 5 is provided with hairbrush 11, filter 10 is located at the below of hairbrush 11 and the two contact, the bottom of the second detritus tank 3 is provided with second except cinder notch 32, second below of removing cinder notch 32 is communicated with the top of the second liquid back pipe 9 and the top of the second liquid back pipe 9 is provided with the second screen cloth 7, first liquid back pipe 8 is all communicated with hydraulic fracture machine or disc mill 1 by main pipe rail with the other end of the second liquid back pipe 9, second detritus tank 3 is provided with good slurry outlet 33.
Further, the outlet of the first detritus tank 2 and the second detritus tank 3 is back taper.This result is beneficial to the sedimentation of slag ball and enrichment, except cinder notch is positioned at back taper structure bottommost,
Further, filter 10 is stainless (steel) wire and the order number of filter 10 is 60 order ~ 200 orders.
The operation principle of this detailed description of the invention is: as shown in Figure 1, and the raw fibre cotton containing slag ball first will be separated from fiber with the compact slag ball of fiber by hydrabrusher or disc mill 1.Hydrabrusher and mill machine 1 can with special manufacturer in contact purchase.Raw fibre need first add water be made into low concentration suspension slurry after enter hydrabrusher or disc mill 1 again.Cotton pulp after hydrabrusher or disc mill 1 are broken up is called " 1 grade of magma ", the first detritus tank 2 is squeezed into by pump, first detritus tank 2 comprises 3 openings, be followed successively by secondary magma outlet 23, one-level magma entrance 21, first from top to bottom except cinder notch 22, secondary magma outlet 23, one-level magma entrance 21, first remove cinder notch 22 and are equipped with Valve controlling aperture.One-level magma entrance 21 removes between cinder notch 22 in secondary magma outlet 23 and first.In operation, the first stirring vane 4 does not stop, and ensures that fiber and slag ball can not fall to bottom simultaneously.Mixing speed should through overtesting and optimization, fiber is suspended due to its less free-falling velocity, thick slag ball can fall to bottom due to its larger free-falling velocity, because thin slag ball free-falling velocity is also very little, so still together suspend with fiber.Optimum mixing speed and mineral fibres chemical composition, geometric parameter are relevant, and also relevant with detritus tank space structure, paddle geometry, the mixing speed of usual first stirring vane 4 is 15 to 100rpm.When slag ball is collected to a certain degree, open first except cinder notch 22 place valve, thick slag ball is expelled to the first screen cloth 6 with water from here and filters, and filtrate returns hydrabrusher after collecting or disc mill 1 is reused.The cotton pulp eliminating thick slag ball is called as " 2 grades of cotton pulps ", to discharge after the first detritus tanks 2, squeeze into the second detritus tank 3 by pump by secondary magma outlet 23.
Second level detritus tank 3 comprises 3 openings, and be followed successively by good slurry outlet 33, secondary magma entrance 31, second from top to bottom except cinder notch 32, each opening part is equipped with Valve controlling aperture.Secondary magma entrance 31 removes between cinder notch 32 in good slurry outlet 33 and second.Filter 10 is fixed on secondary magma entrance less than 31, bottom the back taper of the second detritus tank 3.Second stirring vane 5 is connected to the banister brush that the materials such as polyester are made, hairbrush 11 contacts with filter 10, and the second stirring vane 5 is when rotating, and the surface of band electric brush 11 pairs of filters 10 is cleared up.With similar in the first detritus tank 2, the difference of free-falling velocity is still utilized to be separated.The rotating speed of the second stirring vane 5 should lower than the first stirring vane 4 herein.After 2 grades of magma enter the second detritus tank 3, the mineral fibres that a part of free-falling velocity is less suspends in water, mineral fibres sedimentation together with thin slag ball that another part free-falling velocity is slightly large.When being settled down to filter, because fibre length is longer (according to different production technologies, between 0.3 to 30mm) and cluster appearance usually, a few part is only had to continue sedimentation by filter 10, thin slag ball, then because diameter is less than filter 10 aperture, almost all continues sedimentation by filter 10.The bottom of the second detritus tank 3 is designed to back taper, be beneficial to the sedimentation of slag ball and enrichment, second removes cinder notch 32 is positioned at back taper structure bottommost, when slag ball is collected to a certain degree, open second except cinder notch 32 place valve, thin slag ball and a small amount of fiber are expelled to the second screen cloth 7 with water from here and filter, and filtrate returns hydrabrusher after collecting or disc mill 1 is reused.The fiber be deposited on the second screen cloth 7 stirs rear floating by the hairbrush on the second stirring vane, continues to carry out moving in the second detritus tank 3 until get married and start a new life with water starch outlet outflow.
More than show and describe general principle of the present utility model and principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and description just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (3)
1. a mineral fibres deslagging device, it is characterized in that: it comprises hydraulic fracture machine or disc mill (1), first detritus tank (2), second detritus tank (3), first stirring vane (4), second stirring vane (5), first screen cloth (6), second screen cloth (7), first liquid back pipe (8), second liquid back pipe (9), filter (10), hairbrush (11), hydraulic fracture machine or disc mill (1) are communicated with the one-level magma entrance (21) of the first detritus tank (2) by pipeline, the first stirring vane (4) is provided with in first detritus tank (2), the bottom of the first detritus tank (2) is provided with first except cinder notch (22), first below of removing cinder notch (22) is communicated with the top of the first liquid back pipe (8) and the top of the first liquid back pipe (8) is provided with the first screen cloth (6), secondary magma outlet (23) of the first detritus tank (2) is communicated with secondary magma magma entrance (31) of the second detritus tank (3) by pipeline, the second stirring vane (5) and filter (10) is provided with in second detritus tank (3), second stirring vane (5) is provided with hairbrush (11), filter (10) is located at the below of hairbrush (11) and the two contact, the bottom of the second detritus tank (3) is provided with second except cinder notch (32), second below of removing cinder notch (32) is communicated with the top of the second liquid back pipe (9) and the top of the second liquid back pipe (9) is provided with the second screen cloth (7), first liquid back pipe (8) is all communicated with hydraulic fracture machine or disc mill (1) by main pipe rail with the other end of the second liquid back pipe (9), second detritus tank (3) is provided with good slurry outlet (33).
2. a kind of mineral fibres deslagging device according to claim 1, is characterized in that: the outlet of the first detritus tank (2) and the second detritus tank (3) is back taper.
3. a kind of mineral fibres deslagging device according to claim 1 and 2, is characterized in that: filter (10) is for stainless (steel) wire and the order number of filter (10) is 60 order ~ 200 orders.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520062324.8U CN204448254U (en) | 2015-01-22 | 2015-01-22 | A kind of mineral fibres deslagging device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520062324.8U CN204448254U (en) | 2015-01-22 | 2015-01-22 | A kind of mineral fibres deslagging device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204448254U true CN204448254U (en) | 2015-07-08 |
Family
ID=53655202
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520062324.8U Active CN204448254U (en) | 2015-01-22 | 2015-01-22 | A kind of mineral fibres deslagging device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204448254U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106830668A (en) * | 2017-01-06 | 2017-06-13 | 酒泉恒通节能科技有限公司 | A kind of circulation water law deslagging process during mineral fibre production |
| CN108325735A (en) * | 2017-12-26 | 2018-07-27 | 江苏腾利特种纤维科技有限公司 | The longitudinal rinsing separation device of ceramic fibre and separation method |
| CN110395902A (en) * | 2019-08-20 | 2019-11-01 | 福建德化东芯博新材料科技有限责任公司 | A kind of mineral fibres processing system and its processing method |
| CN114308371A (en) * | 2021-10-25 | 2022-04-12 | 金天环保材料科技(深圳)有限公司 | Metal and nonmetal fine crushing mixture separation device and separation method |
-
2015
- 2015-01-22 CN CN201520062324.8U patent/CN204448254U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106830668A (en) * | 2017-01-06 | 2017-06-13 | 酒泉恒通节能科技有限公司 | A kind of circulation water law deslagging process during mineral fibre production |
| CN106830668B (en) * | 2017-01-06 | 2022-04-08 | 酒泉恒通节能科技有限公司 | Circulating water method deslagging process in mineral fiber production process |
| CN108325735A (en) * | 2017-12-26 | 2018-07-27 | 江苏腾利特种纤维科技有限公司 | The longitudinal rinsing separation device of ceramic fibre and separation method |
| CN110395902A (en) * | 2019-08-20 | 2019-11-01 | 福建德化东芯博新材料科技有限责任公司 | A kind of mineral fibres processing system and its processing method |
| CN110395902B (en) * | 2019-08-20 | 2021-06-29 | 福建德化东芯博新材料科技有限责任公司 | Mineral fiber treatment system and treatment method thereof |
| CN114308371A (en) * | 2021-10-25 | 2022-04-12 | 金天环保材料科技(深圳)有限公司 | Metal and nonmetal fine crushing mixture separation device and separation method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204448254U (en) | A kind of mineral fibres deslagging device | |
| CN105311871A (en) | Novel liquid-solid separation filtering device | |
| CN208234678U (en) | A kind of tailing water sedimentation and thickening machine | |
| CN105879482A (en) | Spiral extruding and sand discharging device for carrying out rotational flow reinforcing and sand removing | |
| CN103638734A (en) | Rotating-platform vacuum filtering machine and filtering method | |
| CN203458887U (en) | Novel disk-type vacuum filter cloth washing device | |
| CN206089096U (en) | Integrative equipment of air floatation precipitation | |
| CN211587110U (en) | Fine sand extractor capable of improving fine sand dehydration efficiency | |
| CN208115288U (en) | Solid-liquid automatic separating apparatus | |
| CN103357622A (en) | Method and equipment for efficiently washing powder or powder materials | |
| CN206229515U (en) | A kind of ore deposit fiber deslagging device | |
| CN205056256U (en) | Processing apricot bao mushroom is with horizontal spiral filtering centrifuge | |
| CN101693155B (en) | Micron or nano grade filter pressing device of dehydration slagging non-pressure vessel | |
| CN103691170A (en) | Conical arc blade-type dynamic filter press | |
| CN202626070U (en) | Corn starch cleaning separator | |
| CN211367209U (en) | Hydraulic cyclone sand removing device | |
| CN209270938U (en) | A kind of petrochemical industry filter device convenient for cleaning | |
| CN209049531U (en) | A kind of high viscosity multifilament slurry fine grinding device | |
| CN208829527U (en) | A kind of thickener constant-current stabilizer | |
| CN206721561U (en) | It is a kind of to improve the system for removing paper pulp impurity efficiency | |
| CN209501971U (en) | A kind of polarization polymerization removes the device of microparticle in liquid | |
| CN207576682U (en) | A kind of Whirlwind wet collector | |
| CN207253849U (en) | The sieve energy-efficient mud and water separating equipment of filtering type is dropped down in a kind of bucket storehouse | |
| CN201524480U (en) | Micron-grade or nanometer-grade pressure filter of dehydration and deslagging non-pressure vessel | |
| CN208486122U (en) | A kind of biconial scummer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |