CN201783343U - Grinding separator - Google Patents
Grinding separator Download PDFInfo
- Publication number
- CN201783343U CN201783343U CN2010201980339U CN201020198033U CN201783343U CN 201783343 U CN201783343 U CN 201783343U CN 2010201980339 U CN2010201980339 U CN 2010201980339U CN 201020198033 U CN201020198033 U CN 201020198033U CN 201783343 U CN201783343 U CN 201783343U
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- CN
- China
- Prior art keywords
- separator
- pulverizer
- primary
- mesh belt
- pulverizers
- 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.)
- Expired - Fee Related
Links
- 238000000227 grinding Methods 0.000 title abstract description 4
- 230000005540 biological transmission Effects 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000001914 filtration Methods 0.000 claims abstract description 4
- 238000000926 separation method Methods 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 7
- 238000007670 refining Methods 0.000 claims description 6
- 238000001125 extrusion Methods 0.000 claims description 4
- 230000002093 peripheral effect Effects 0.000 claims 1
- 239000002893 slag Substances 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 2
- 239000000463 material Substances 0.000 description 8
- 229920002472 Starch Polymers 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
Images
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
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- Crushing And Pulverization Processes (AREA)
Abstract
Description
一、所属的技术领域1. Technical field
本实用新型涉及一种磨浆分离机。 The utility model relates to a pulp refining and separating machine. the
二、背景技术2. Background technology
目前,磨浆分离机的种类很多,大多数的磨浆分离机均由粉碎部件、分离部件、传动部件和供水部件组成。其粉碎多为一级粉碎,多采用刨丝机、锤片式粉碎机、刮爪式粉碎机、砂轮磨等,这种只有一级粉碎的设备要么存在能耗高,要么粉碎不够细,提取率低,当前也有采用两级粉碎的,比如本人的实用新型专利2004200514257所公开的一种淀粉加工设备,其二级粉碎采用刀片式粉碎,效果较差,淀粉分离率低,只适合于粗纤维物的加工。 At present, there are many types of pulp separators, most of which are composed of crushing parts, separation parts, transmission parts and water supply parts. The crushing is mostly one-stage crushing, and shredders, hammer mills, scraper-claw grinders, grinding wheel mills, etc. are mostly used. This kind of equipment with only one-stage crushing either has high energy consumption, or the crushing is not fine enough, and the extraction The rate is low, and there are currently two-stage crushing, such as a kind of starch processing equipment disclosed in my utility model patent 2004200514257. The secondary crushing adopts blade crushing, the effect is poor, and the starch separation rate is low, which is only suitable for crude fiber processing of things. the
本实用新型的目的在于针对上述磨浆分离机存在的问题,提供一种粉碎、分离于一体、能耗低、结构紧凑、物料分离率高的磨浆分离机。 The purpose of the utility model is to solve the problems existing in the above-mentioned refining and separating machine, and provide a refining and separating machine which integrates crushing and separation, has low energy consumption, compact structure and high material separation rate. the
三、实用新型的内容 3. Contents of utility models
实现上述目的的技术方案是:一种磨浆分离机,它由机架、传动部件、供水部件、粉碎器和过滤分离系统组成,其特征在于:它采用两级粉碎器,一级粉碎器的位于一级分离器的上面,一级粉碎器的出料口与一级分离器的进料口相通,一级分离器的出渣口与二级粉碎器的进料口相通,二级粉碎器位于二级分离器的上面,二级粉碎器的出料口与二级分离器的进料口相通。 The technical solution to achieve the above purpose is: a pulp refining separator, which is composed of a frame, a transmission part, a water supply part, a pulverizer and a filtration separation system, and is characterized in that it adopts two-stage pulverizers, and the first-stage pulverizer Located on the top of the primary separator, the discharge port of the primary separator communicates with the feed port of the primary separator, the slag discharge port of the primary separator communicates with the feed port of the secondary grinder, and the secondary grinder Located above the secondary separator, the discharge port of the secondary pulverizer communicates with the feed port of the secondary separator. the
本实用新型有以下优点: The utility model has the following advantages:
1、二级粉碎采用锤片式粉碎,物料粉碎率高; 1. The secondary crushing adopts hammer crushing, and the material crushing rate is high;
2、采用粉碎和分离交替进行,物料分离更为容易; 2. The crushing and separation are alternately carried out, and the separation of materials is easier;
3、一级分离去除部分物料,减少阻滞力,动力消耗小; 3. One-stage separation removes part of the material, reduces the blocking force, and reduces power consumption;
4、集粉碎、分离于一机,结构更紧凑,占地面积小。 4. Combining crushing and separation in one machine, the structure is more compact and the floor space is small. the
四、附图说明4. Description of drawings
以下结合附图对本实用新型的几种优选实施例进行具体描述,其中: Below in conjunction with accompanying drawing several preferred embodiments of the present utility model are specifically described, wherein:
图1是本实用新型的一种侧面图,局部被剖开; Fig. 1 is a kind of side view of the utility model, and part is cut away;
图2是本实用新型的一种正视结构示意图,局部被剖开; Fig. 2 is a kind of front view structure schematic diagram of the present utility model, part is cut away;
图3是本实用新型的具体实例图; Fig. 3 is the concrete example figure of the present utility model;
图4是本实用新型的又一具体实例图。 Fig. 4 is another concrete example figure of the utility model. the
五、具体实施方式5. Specific implementation
如图1和图2所示的一种磨浆分离机,它由机架1、传动部件3、供水部件4、粉碎器和过滤分离系统组成,其中一级粉碎器5是刨丝式粉碎机,位于一级分离器6的上面,一级分离器6是卧式搅拌分离器,由搅拌转子61和滤网62等构成,一级粉碎器5的出料口与一级分离器6的进料口相通,一级分离器6的出料口与二级粉碎器7的进料口相通,二级粉碎器7是锤片式粉碎器,它主要由多组锤片71,圆盘转子72,筛板73构成,二级粉碎器7位于二级分离器8的上面,二级分离器8也是卧式搅拌分离器,二级粉碎器7的出料口与二级分离器8的进料口相通。供水系统的设置是比较灵活的,它有多个供水出口,一般位于一级分离器的上方,二级粉碎器的上方,对一级粉碎后的物料加水搅拌,以便更好的分离。在图3中,二级分离器8的出料口9与其它分离器10相连通,以对过滤后的物料进行进一步的分离,以提高分离净率。 As shown in Figure 1 and Figure 2, a pulp separator is composed of a frame 1, a transmission part 3, a water supply part 4, a pulverizer and a filtration separation system, wherein the primary pulverizer 5 is a shredded pulverizer , located on the top of the primary separator 6, the primary separator 6 is a horizontal stirring separator, which is composed of a stirring rotor 61 and a filter screen 62, etc., the discharge port of the primary pulverizer 5 and the inlet of the primary separator 6 The feed port is connected, and the discharge port of the primary separator 6 is connected with the feed port of the secondary pulverizer 7. The secondary pulverizer 7 is a hammer pulverizer, which mainly consists of multiple sets of hammer blades 71, a disc rotor 72 , constituted by a sieve plate 73, the secondary pulverizer 7 is located on the top of the secondary separator 8, the secondary separator 8 is also a horizontal stirring separator, the discharge port of the secondary pulverizer 7 and the feed of the secondary separator 8 The mouth communicates. The setting of the water supply system is relatively flexible. It has multiple water supply outlets, which are generally located above the primary separator and above the secondary pulverizer. Water is added to the primary pulverized material for better separation. In FIG. 3 , the outlet 9 of the secondary separator 8 is connected with other separators 10 to further separate the filtered material and improve the separation rate. the
在图3中,二级粉碎器有两个,两个二级粉碎器7均为锤片式粉碎器,它们的中心轴在一条直线上,传动皮带轮位于机架的两侧。两个二级粉碎器7的进料口与一级过滤器6的出口相通,它们都位于二级分离器8的上方,出料口 入二级分离器8的进料口相同,二级粉碎后的物料都进入二级分离器8进行分离。 In Fig. 3, there are two secondary pulverizers, two secondary pulverizers 7 are hammer pulverizers, their central axis is on a straight line, and the transmission pulley is positioned at both sides of the frame. The feed inlet of two secondary pulverizers 7 is communicated with the outlet of primary filter 6, and they are all positioned at the top of secondary separator 8, and discharge port enters the same feed inlet of secondary separator 8, and secondary pulverization The final materials all enter the secondary separator 8 for separation. the
在图4中,二级分离器8的出料口9,与曲网挤压式的分离器相连,它由多个淘洗搅拌分离器11、多个挤压辊12及过滤输送网带13、转角辊14,及网带调整器15组成,各淘洗搅拌分离器11和挤压辊12间隔布置,都固定在机架上,过滤输送网带13在转角辊14的支撑下包裹挤压辊12的部分圆周面,过滤输送网带13在传动机构带动下不停的运转,在过滤输送网带13上面,各个分离器出料口和挤压辊中间的部位装有导流板15,导流板15作用主要是防止分离后的物料流出过滤输送网带13。 In Fig. 4, the outlet 9 of the secondary separator 8 is connected to the separator of the curved net extruding type, and it is composed of a plurality of
以上所述的仅是本实用新型的优选方案,应当同指出,对于本领域的普通技术人员来说,在不脱离本实用新型原理的前提下,还可以做出若干变型和改进,也应视为属于本实用新型的保护范围。 The above is only the preferred version of the utility model, and it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the utility model, some modifications and improvements can also be made. For belonging to the scope of protection of the present utility model. the
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010201980339U CN201783343U (en) | 2010-05-16 | 2010-05-16 | Grinding separator |
Applications Claiming Priority (1)
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CN2010201980339U CN201783343U (en) | 2010-05-16 | 2010-05-16 | Grinding separator |
Publications (1)
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CN201783343U true CN201783343U (en) | 2011-04-06 |
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CN2010201980339U Expired - Fee Related CN201783343U (en) | 2010-05-16 | 2010-05-16 | Grinding separator |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104151437A (en) * | 2014-07-31 | 2014-11-19 | 马英 | Double-layered pulverizer for potatoes |
CN106397613A (en) * | 2016-11-22 | 2017-02-15 | 郑州诚合信息技术有限公司 | Sweet potato starch production integrated apparatus |
CN114226020A (en) * | 2021-12-22 | 2022-03-25 | 禹州市新业水利机械制造有限公司 | Multistage slurry grinding pump with solid-liquid separation mechanism |
-
2010
- 2010-05-16 CN CN2010201980339U patent/CN201783343U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104151437A (en) * | 2014-07-31 | 2014-11-19 | 马英 | Double-layered pulverizer for potatoes |
CN104151437B (en) * | 2014-07-31 | 2016-08-24 | 马英 | The compound powder remover of potato class |
CN106397613A (en) * | 2016-11-22 | 2017-02-15 | 郑州诚合信息技术有限公司 | Sweet potato starch production integrated apparatus |
CN114226020A (en) * | 2021-12-22 | 2022-03-25 | 禹州市新业水利机械制造有限公司 | Multistage slurry grinding pump with solid-liquid separation mechanism |
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Legal Events
Date | Code | Title | Description |
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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 |
Granted publication date: 20110406 Termination date: 20150516 |
|
EXPY | Termination of patent right or utility model |