CN110667163A - Screw propulsion type high-pressure solid-liquid separator - Google Patents
Screw propulsion type high-pressure solid-liquid separator Download PDFInfo
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- CN110667163A CN110667163A CN201911087696.5A CN201911087696A CN110667163A CN 110667163 A CN110667163 A CN 110667163A CN 201911087696 A CN201911087696 A CN 201911087696A CN 110667163 A CN110667163 A CN 110667163A
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- 239000007788 liquid Substances 0.000 title claims abstract description 61
- 238000001125 extrusion Methods 0.000 claims abstract description 118
- 230000001681 protective effect Effects 0.000 claims abstract description 30
- 230000003014 reinforcing effect Effects 0.000 claims abstract description 22
- 230000002787 reinforcement Effects 0.000 claims description 60
- 230000000903 blocking effect Effects 0.000 claims description 8
- 239000000463 material Substances 0.000 abstract description 45
- 238000000034 method Methods 0.000 abstract description 17
- 230000008569 process Effects 0.000 abstract description 16
- 238000000926 separation method Methods 0.000 abstract description 8
- 230000018044 dehydration Effects 0.000 abstract description 6
- 238000006297 dehydration reaction Methods 0.000 abstract description 6
- 238000013461 design Methods 0.000 abstract description 5
- 238000012423 maintenance Methods 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 230000008859 change Effects 0.000 abstract description 2
- 230000003139 buffering effect Effects 0.000 abstract 1
- 230000003467 diminishing effect Effects 0.000 abstract 1
- 239000004744 fabric Substances 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 8
- 210000003608 fece Anatomy 0.000 description 6
- 239000010871 livestock manure Substances 0.000 description 6
- 125000006850 spacer group Chemical group 0.000 description 6
- 241000283690 Bos taurus Species 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000004323 axial length Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/12—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
- B30B9/121—Screw constructions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B15/00—Details of, or accessories for, presses; Auxiliary measures in connection with pressing
- B30B15/28—Arrangements for preventing distortion of, or damage to, presses or parts thereof
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/12—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
- B30B9/14—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing operating with only one screw or worm
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/26—Permeable casings or strainers
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Abstract
Description
技术领域technical field
本发明涉及一种螺旋推进式高压固液分离机,属于固液分离装置技术领域。The invention relates to a screw-propelled high-pressure solid-liquid separator, which belongs to the technical field of solid-liquid separation devices.
背景技术Background technique
生产牛床垫料需要用到牛的粪便,且需要对粪污进行处理,以便生产无菌的牛床垫料。固液分离工艺是在畜禽粪污处理,使之达到无害化、资源化要求过程中,不可或缺的技术环节。目前,国内外固液分离技术主要将高含水率(>80%)的细碎物料均匀脱水成低含水率物料(约55%)需要两台固液分离机,其工作方式为首先用一台低功率固液分离机先对含水率80%以上的物料进行初级挤压,使物料含水率降至70%左右,然后再用一台或一台以上的大功率固液分离机对70%含水率的物料进行二次挤压脱水方可获得60%左右的低含水率物料。这样不仅脱水过程的能耗很大,而且一次和二次固液分离机的生产效率不易匹配,需要通过操作人员不断调整两级设备的运行速度或使用自动检测系统进行自动协调,但无论如何这都增加了设备成本以及生产过程的设备故障几率。这也是目前此类工作的难题。The production of cattle bedding material requires the use of cow manure, and the manure needs to be treated in order to produce sterile cattle bedding material. The solid-liquid separation process is an indispensable technical link in the process of livestock and poultry manure treatment, so that it can meet the requirements of harmlessness and resource utilization. At present, the solid-liquid separation technology at home and abroad mainly dehydrates finely crushed materials with high moisture content (>80%) into materials with low moisture content (about 55%), which requires two solid-liquid separators. The high-power solid-liquid separator first performs primary extrusion on the material with a moisture content of more than 80% to reduce the moisture content of the material to about 70%, and then uses one or more high-power solid-liquid separators to 70% moisture content. The material with low moisture content of about 60% can be obtained by secondary extrusion and dehydration. In this way, not only the energy consumption of the dehydration process is large, but also the production efficiency of the primary and secondary solid-liquid separators is not easy to match. It is necessary to continuously adjust the operating speed of the two-stage equipment by the operator or use the automatic detection system for automatic coordination, but in any case, this Both increase the cost of equipment and the probability of equipment failure in the production process. This is also the current problem of this type of work.
之前发明人设计的变截面螺杆固液分离机,虽然解决了上述问题,但是在实际生产使用过程中,由于螺旋挤压推进杆和防护罩的截面由大变小,很容易造成物料的阻塞,而且机器能耗大,挤压过程对设备的损耗很大,而且挤压中的物料对筛网损坏也很大,设备需要经常维修。Although the variable-section screw solid-liquid separator designed by the inventor before solved the above problems, in the actual production and use process, the cross-section of the screw extrusion rod and the protective cover changed from large to small, which easily caused material blockage. Moreover, the machine consumes a lot of energy, the extrusion process consumes a lot of equipment, and the material in the extrusion process is also very damaged to the screen, and the equipment needs frequent maintenance.
发明内容SUMMARY OF THE INVENTION
本发明为解决现有技术的固液分离机脱水过程的能耗很大,而且一次和二次固液分离机的生产效率不易匹配,需要通过操作人员不断调整两级设备的运行速度或使用自动检测系统进行自动协调,增加了设备成本以及生产过程的设备故障几率的问题以及在实际生产使用过程中,由于螺旋挤压推进杆和防护罩的截面由大变小,很容易造成物料的阻塞,而且机器能耗大,挤压过程对设备的损耗很大,而且挤压中的物料对筛网损坏也很大,设备需要经常维修,提出一种螺旋推进式高压固液分离机,螺旋挤压推进杆和防护罩采用非变截面设计,设计了分隔区作为缓冲,避免了之前变截面设计导致的物料堵塞造成的机器卡死状况,能耗更低,脱水过程更加顺畅。In order to solve the problem that the dehydration process of the solid-liquid separator in the prior art consumes a lot of energy, and the production efficiency of the primary and secondary solid-liquid separators is not easy to match, the operator needs to continuously adjust the running speed of the two-stage equipment or use automatic The automatic coordination of the detection system increases the equipment cost and the probability of equipment failure in the production process. In the actual production and use process, because the cross-section of the screw extrusion rod and the protective cover changes from large to small, it is easy to cause material blockage. In addition, the machine consumes a lot of energy, the extrusion process consumes a lot of equipment, and the material in extrusion is also very damaged to the screen, and the equipment needs frequent maintenance. A screw-propelled high-pressure solid-liquid separator is proposed. The propulsion rod and protective cover are designed with non-variable cross-section, and a partition area is designed as a buffer, which avoids the jamming of the machine caused by the material blockage caused by the previous design of variable cross-section. The energy consumption is lower, and the dehydration process is smoother.
本发明提出一种螺旋推进式高压固液分离机包括进料口、溢流口、缓冲室、阻滞挡板、调整螺杆、筛网、集液槽、驱动装置、螺旋挤压推进杆、防护罩、排液口、出料口、筛网加固框架、前端夹固机构和若干可替换活接轴套;所述防护罩内纵向安装有螺旋挤压推进杆,所述螺旋挤压推进杆外周安装有筛网,所述筛网通过筛网加固框架与防护罩固连,所述防护罩的一端设置有驱动装置,驱动螺旋挤压推进杆转动,另一端设置有出料口,所述出料口的前端通过调整螺杆固定有阻滞挡板,所述螺旋挤压推进杆分为不连续的两段,分别为初步挤压段和二次挤压段,所述防护罩的左侧上方安装有缓冲室,所述缓冲室上安装有进料口和溢流口,所述防护罩的底部设置有漏孔,所述防护罩的下方安装有集液槽,所述集液槽下方设置有排液口;The invention proposes a screw-propelled high-pressure solid-liquid separator comprising a feed port, an overflow port, a buffer chamber, a blocking baffle, an adjusting screw, a screen, a liquid collecting tank, a driving device, a screw extrusion rod, a protection A cover, a liquid discharge port, a discharge port, a screen reinforcement frame, a front-end clamping mechanism and a number of replaceable articulated bushings; a screw extrusion push rod is longitudinally installed in the protective cover, and the outer circumference of the screw extrusion push rod is installed A screen is installed, and the screen is fixedly connected with the protective cover through the screen reinforcement frame. One end of the protective cover is provided with a driving device, which drives the screw extrusion push rod to rotate, and the other end is provided with a discharge port. The front end of the material port is fixed with a blocking baffle by adjusting the screw. The screw extrusion push rod is divided into two discontinuous sections, namely the primary extrusion section and the secondary extrusion section. The upper left side of the protective cover is A buffer chamber is installed, a feed port and an overflow port are installed on the buffer chamber, a leak hole is arranged at the bottom of the protective cover, a liquid collecting tank is installed under the protective cover, and a liquid collecting tank is installed below the There is a drain port;
所述螺旋挤压推进杆的通轴外套有若干可替换活接轴套,所述螺旋挤压推进杆的二次挤压段和若干可替换活接轴套能从通轴上取下并变换位置,所述通轴的前端通轴伸出防护罩并在端头安装有前端夹固结构,用于紧固螺旋挤压推进杆的二次挤压段和若干可替换活接轴套。The through shaft sleeve of the screw extrusion push rod has several replaceable articulated shaft sleeves, and the secondary extrusion section of the screw extrusion push rod and several replaceable articulated shaft sleeves can be removed from the through shaft and changed. position, the front end of the through shaft extends out of the protective cover, and a front end clamping structure is installed at the end, which is used to fasten the secondary extrusion section of the screw extrusion push rod and several replaceable articulated bushings.
优选地,所述防护罩内纵向依次分隔为进料区、初步挤压区、间隔区、二次挤压区和出料区,所述螺旋挤压推进杆的初步挤压段位于初步挤压区,二次挤压段位于二次挤压区。Preferably, the protective cover is longitudinally divided into a feeding area, a preliminary extrusion area, a spacing area, a secondary extrusion area and a discharge area, and the preliminary extrusion section of the screw extrusion push rod is located in the preliminary extrusion area. The secondary extrusion section is located in the secondary extrusion zone.
优选地,所述螺旋挤压推进杆的螺旋外径为250~280mm,内径为120~160mm,推进叶片为双螺旋,螺旋挤压推进杆的升角为5~20度,轴向长度为700~900mm。Preferably, the helical outer diameter of the screw extrusion rod is 250-280 mm, the inner diameter is 120-160 mm, the propulsion blade is a double helix, the lift angle of the screw extrusion rod is 5-20 degrees, and the axial length is 700 mm. ~900mm.
优选地,所述螺旋挤压推进杆的初步挤压段和二次挤压段的长度为500~900mm,出料区的长度为200~400mm。Preferably, the length of the primary extrusion section and the secondary extrusion section of the screw extrusion push rod is 500-900 mm, and the length of the discharge area is 200-400 mm.
优选地,所述筛网加固框架包括上筛网加固结构和下筛网加固结构,所述上筛网加固结构和下筛网加固结构的结构相同,为半圆筒结构,所述上筛网加固结构安装在下筛网加固结构上方形成一个圆筒结构;所述上筛网加固结构包括若干加固环肋、若干加固纵肋、两个端法兰、两个纵法兰和加强孔板,所述筛网安装于上筛网加固结构内表面,所述筛网的外周安装有加强孔板,所述筛网和加强孔板上分布有很多小孔,所述加强孔板的外周纵向安装有若干加固纵肋,横向安装有若干加固环肋,若干所述加固纵肋的两端安装有端法兰,若干所述加固环肋的两端安装有纵法兰,所述上筛网加固结构和下筛网加固结构通过纵法兰固定连接。Preferably, the screen reinforcement frame includes an upper screen reinforcement structure and a lower screen reinforcement structure, the upper screen reinforcement structure and the lower screen reinforcement structure are the same in structure and are semi-cylindrical structures, and the upper screen reinforcement The structure is installed above the lower screen reinforcement structure to form a cylindrical structure; the upper screen reinforcement structure includes a number of reinforcement ring ribs, a number of reinforcement longitudinal ribs, two end flanges, two longitudinal flanges and a reinforcement orifice plate. The screen is installed on the inner surface of the upper screen reinforcement structure, the outer periphery of the screen is equipped with a reinforcing orifice plate, the screen and the reinforcing orifice plate are distributed with many small holes, and the outer periphery of the reinforcing orifice plate is longitudinally installed with a number of small holes. Reinforcing longitudinal ribs, a number of reinforcement ring ribs are installed laterally, end flanges are installed at both ends of the reinforcement longitudinal ribs, longitudinal flanges are installed at both ends of the reinforcement ring ribs, and the upper screen reinforcement structure and The reinforcement structure of the lower screen is fixedly connected by the longitudinal flange.
优选地,所述加强孔板紧贴筛网的外表面。Preferably, the reinforcing orifice plate is in close contact with the outer surface of the screen.
优选地,所述筛网上小孔的孔径为2.5-3.5mm,网壁厚为2-4mm,孔间距为4-7mm。Preferably, the aperture of the small holes on the screen is 2.5-3.5mm, the mesh wall thickness is 2-4mm, and the hole spacing is 4-7mm.
优选地,所述加强孔板的厚度为5-15mm。Preferably, the thickness of the reinforcing orifice plate is 5-15mm.
优选地,所述加强孔板上小孔的孔径为25-30mm,孔间距为35-40mm。Preferably, the diameter of the small holes on the reinforced orifice plate is 25-30 mm, and the spacing between the holes is 35-40 mm.
优选地,所述前端夹固结构包括固定板和若干螺钉,所述固定板通过若干螺钉固定在通轴的端头。Preferably, the front-end clamping structure includes a fixing plate and a plurality of screws, and the fixing plate is fixed on the end of the through shaft by a plurality of screws.
本发明所述的螺旋推进式高压固液分离机的有益效果为:The beneficial effects of the screw-propelled high-pressure solid-liquid separator of the present invention are:
1、本发明所述的螺旋推进式高压固液分离机的螺旋挤压推进杆和防护罩采用非变截面设计,加工工艺简单,中间设置了间隔区作为缓冲,避免了之前变截面设计导致的物料堵塞造成的机器卡死状况;1. The screw extrusion rod and the protective cover of the screw-propelled high-pressure solid-liquid separator of the present invention adopt a non-variable section design, the processing technology is simple, and a spacer is set in the middle as a buffer, which avoids the previous design of the variable section. The machine is stuck due to material blockage;
2、本发明所述的螺旋推进式高压固液分离机可以一次性地完成从90%粪污液体进入设备,出料时干物质的含水率在60%以下,设置间隔区,能耗更低,脱水过程更加顺畅;2. The screw-propelled high-pressure solid-liquid separator of the present invention can complete the entry of 90% of the manure liquid into the equipment at one time, and the moisture content of the dry matter is below 60% when discharging. , the dehydration process is smoother;
3、本发明所述的螺旋推进式高压固液分离机相比传统的二次固液分离机更加省地,解决了一次、二次固液分离机处理速度不好匹配还需增加之间的调配环节的问题;3. Compared with the traditional secondary solid-liquid separator, the screw-propelled high-pressure solid-liquid separator of the present invention is more cost-effective, and solves the problem that the processing speeds of the primary and secondary solid-liquid separators are not well matched and need to be increased. problems in the deployment process;
4、本发明所述的螺旋推进式高压固液分离机其作用在于使含水率大于80%有机细碎物料经其挤压一次脱水即可使其含水率降至50~55%,这种固液分离机的结构紧凑,仅需一个动力源即可完成全部低含水率物料的生产,没有之前那种人为或自动控制环节,设备简洁、节能、高效;4. The function of the screw-propelled high-pressure solid-liquid separator of the present invention is to reduce the moisture content of the organic finely crushed materials to 50-55% by extruding and dehydrating the organic finely divided materials with a moisture content greater than 80%. The structure of the separator is compact, and only one power source can complete the production of all materials with low moisture content. There is no manual or automatic control link like the previous one, and the equipment is simple, energy-saving and efficient;
5、本发明所述的螺旋推进式高压固液分离机的筛网加固框架和二级筛网分为两个半圆筒部分,通过法兰连接成一体,拆卸和维护方便;5. The screen reinforcement frame and the secondary screen of the screw-propelled high-pressure solid-liquid separator of the present invention are divided into two semi-cylindrical parts, which are connected by flanges into one body, which is convenient for disassembly and maintenance;
6、本发明所述的螺旋推进式高压固液分离机的筛网加固框架采用加强结构,可以抵抗高压固液分离设备的高压,加固筛网,保证筛网长时间的工作。6. The screen reinforcement frame of the screw-propelled high-pressure solid-liquid separator of the present invention adopts a reinforced structure, which can resist the high pressure of the high-pressure solid-liquid separation equipment, strengthen the screen, and ensure the long-term operation of the screen.
附图说明Description of drawings
图1是本发明所述的螺旋推进式高压固液分离机的结构示意图;Fig. 1 is the structural representation of the screw-propelled high-pressure solid-liquid separator of the present invention;
图2是本发明所述的螺旋推进式高压固液分离机的工作流程图;Fig. 2 is the working flow chart of the screw-propelled high-pressure solid-liquid separator of the present invention;
图3是本发明所述的螺旋挤压推进杆和可替换活接轴套减小间隔区距离的示意图;3 is a schematic diagram of the screw extrusion push rod and the replaceable articulated bushing of the present invention to reduce the distance of the interval;
图4是本发明所述的螺旋挤压推进杆和可替换活接轴套调节间隔区距离的示意图;4 is a schematic diagram of the screw extrusion push rod and the replaceable articulated bushing according to the present invention for adjusting the distance of the interval;
图5是本发明所述的筛网加固框架的结构示意图;Fig. 5 is the structural representation of the screen reinforcement frame of the present invention;
图中:1-进料口;2-溢流口;3-缓冲室;4-进料区;5-初步挤压区;6-间隔区;7-二次挤压区;8-阻滞挡板;9-出料区;10-调整螺杆;11-筛网;12-集液槽;13-可替换活接轴套;14-驱动电机;15-螺旋挤压推进杆;16-防护罩;17-减速机;18-排液口;20-筛网加固框架;201-加固环肋;202-加固纵肋;203-端法兰;204-纵法兰;205-加强孔板;21-通轴;22-前端夹固结构。In the figure: 1-feed port; 2-overflow port; 3-buffer chamber; 4-feed zone; 5-preliminary extrusion zone; 6-spacer zone; 7-secondary extrusion zone; 8-block Baffle; 9-discharge area; 10-adjustment screw; 11-screen; 12-liquid collection tank; 13-replaceable joint bushing; 14-drive motor; 15-screw extrusion push rod; 16-protection hood; 17- reducer; 18- drain; 20- screen reinforced frame; 201- reinforced ring rib; 202- reinforced longitudinal rib; 203- end flange; 204- longitudinal flange; 205- reinforced orifice plate; 21-Through shaft; 22-Front end clamping structure.
具体实施方式Detailed ways
以下结合附图对本发明的具体实施方式作进一步详细的说明:The specific embodiments of the present invention will be described in further detail below in conjunction with the accompanying drawings:
具体实施方式一:参见图1-图5说明本实施方式。本实施方式所述的螺旋推进式高压固液分离机包括进料口1、溢流口2、缓冲室3、阻滞挡板8、调整螺杆10、筛网11、集液槽12、驱动装置、螺旋挤压推进杆15、防护罩16、排液口18、筛网加固框架20、前端夹固结构22和若干可替换活接轴套13;所述防护罩16内纵向安装有螺旋挤压推进杆15,所述螺旋挤压推进杆15外周安装有筛网11,所述筛网11通过筛网加固框架20与防护罩16固连,所述防护罩16的一端设置有驱动装置,驱动螺旋挤压推进杆15转动,另一端设置有出料口,所述出料口的前端通过调整螺杆10固定有阻滞挡板8,所述螺旋挤压推进杆15分为不连续的两段,分别为初步挤压段和二次挤压段,所述防护罩16的左侧上方安装有缓冲室3,所述缓冲室3上安装有进料口1和溢流口2,所述防护罩16的底部设置有漏孔,所述防护罩16的下方安装有集液槽12,所述集液槽12下方设置有排液口18;所述螺旋挤压推进杆15的通轴21外套有若干可替换活接轴套13,所述螺旋挤压推进杆15的二次挤压段和若干可替换活接轴套13能从通轴21上取下并变换位置,所述螺旋挤压推进杆15的前端通轴21伸出防护罩16并在端头安装有前端夹固结构22,用于紧固螺旋挤压推进杆15的二次挤压段和若干可替换活接轴套13。凡有螺旋挤压推进杆15的区间,紧贴叶片外设置筛网11,挤出的废液透过筛网11进入集液槽12经排液口18排出。Embodiment 1: This embodiment is described with reference to FIG. 1 to FIG. 5 . The screw-propelled high-pressure solid-liquid separator described in this embodiment includes a feed port 1, an overflow port 2, a buffer chamber 3, a blocking
所述防护罩16内纵向依次分隔为进料区4、初步挤压区5、间隔区6、二次挤压区7和出料区9,所述螺旋挤压推进杆15的初步挤压段位于初步挤压区5,二次挤压段位于二次挤压区7。The
所述螺旋挤压推进杆15的螺旋外径为350~450mm,所述通轴21直径(也就是螺旋外径)为150~250mm,推进叶片为单螺旋,螺旋挤压推进杆15的升角为5~16度。The outer diameter of the
所述螺旋挤压推进杆15的初步挤压段和二次挤压段的长度为500~900mm,出料区9的长度为200~400mm。The length of the primary extrusion section and the secondary extrusion section of the screw
所述前端夹固结构22包括固定板和若干螺钉,所述固定板通过若干螺钉固定在通轴的端头。The front-
本发明的要点在于将螺旋挤压推进杆15上的螺旋叶片分成两段不连续结构,分别为初步挤压段和二次挤压段,两段螺旋叶片分别对应在初步挤压区5和二次挤压区7,初步挤压段的螺旋叶片螺距较大,二次挤压段的螺旋叶片螺距较小,两段之间断开一定距离,即间隔区6,使初步挤压的物料有一定的堆积过程从而使高含水率的物料得到初步的固液分离。The gist of the present invention is to divide the helical blades on the helical
当物料推进到二次挤压区7时,因为二次挤压段的螺旋叶片的螺距较小物料推进的速度较慢,这样便使物料在一次挤压和二次挤压叶片间的断开的距离之间得到进一步压缩,这样我们有望得到70%左右含水率的物料,基本上达到一次固液分离机的功能。When the material is advanced to the secondary extrusion zone 7, because the pitch of the helical blades of the secondary extrusion section is smaller, the material advancing speed is slower, so that the material is disconnected between the primary extrusion and the secondary extrusion blade. The distance between them is further compressed, so that we can expect to obtain materials with a moisture content of about 70%, which basically achieves the function of a solid-liquid separator.
经一步挤压后体积被压缩了的物料进入到二次挤压区7后,由于二次挤压段螺旋叶片的推进速度较小、但是推力较大,可进一步对物料施加挤压力,当物料被推至出料区9后,由于出料口9前端的阻滞挡板8的作用又进一步加大了对物料的挤压力,物料中的水分被进一步通过出料区9的筛网排出。After the one-step extrusion, the volume-compressed material enters the secondary extrusion zone 7. Since the propulsion speed of the spiral blades in the secondary extrusion section is small, but the thrust is large, the extrusion force can be further applied to the material. After the material is pushed to the
但在一次二次螺旋叶片的断开的长度(即间隔区6)多少才能恰好使最终的物料的含水率达到想要的程度是非常关键的。因此本案在螺旋挤压推进杆15上设计了一种可变叶片间距的轴套,将与螺旋叶片内径相同的几段不同长度的可替换活接轴套13套于通轴21上,通过改变可替换活接轴套13与两段螺旋叶片的相对位置来改变间隔区6的距离,直到得到满意的含水率的物料,最终的物料含水率控制50~60%之间However, it is very critical how much the broken length of the primary and secondary helical blades (ie the spacer 6) can just make the moisture content of the final material reach the desired level. Therefore, in this case, a variable blade spacing bushing is designed on the screw
调节间隔区6间距的操作原理如下:位于二次挤压区7的螺旋叶片与位于初步挤压区5的螺旋叶片是断开的,它们同时套在一个通轴21上,同时若干短的可替换活接轴套13也套在通轴21上,可以将二次挤压区7的螺旋叶片从通轴21上取下,然后增加或减少间隔区6之间的可替换活接轴套13这样就改变了间隔区6的间距。而从间隔区6取下的可替换活接轴套13就通过前端夹固结构22固定在在螺旋叶片的前端(出料口端),这样,套在通轴21上的叶片与可替换活接轴套13的总和并没有变;当要增加间隔区6的间距时,将二次挤压区7的叶片前端的可替换活接轴套13一起取下,再把前端的可替换活接轴套13先套在通轴21上,然后再套上螺旋叶片15的二次挤压段,这样间隔区6的距离就增加了,而此时套在通轴21上的螺旋叶片15和可替换活接轴套13的总数和长度不变。The operating principle of adjusting the spacing of the
所述筛网加固框架20包括上筛网加固结构和下筛网加固结构,所述上筛网加固结构和下筛网加固结构的结构相同,为半圆筒结构,所述上筛网加固结构安装在下筛网加固结构上方形成一个圆筒结构;所述筛网11分为上下两半,分别安装于上筛网加固结构和下筛网加固结构内表面,所述上筛网加固结构包括若干加固环肋201、若干加固纵肋202、两个端法兰203、两个纵法兰204和加强孔板205,所述筛网11安装于上筛网加固结构内表面,所述筛网11的外周安装有加强孔板205,所述筛网11和加强孔板205上分布有很多小孔,所述加强孔板205的外周纵向安装有若干加固纵肋202,横向安装有若干加固环肋201,若干所述加固纵肋202的两端安装有端法兰203,若干所述加固环肋201的两端安装有纵法兰204,所述上筛网加固结构和下筛网加固结构通过纵法兰204固定连接。The screen reinforcement frame 20 includes an upper screen reinforcement structure and a lower screen reinforcement structure. The upper screen reinforcement structure and the lower screen reinforcement structure have the same structure and are semi-cylindrical structures. The upper screen reinforcement structure is installed. A cylindrical structure is formed above the lower screen reinforcement structure; the screen 11 is divided into upper and lower halves, which are respectively installed on the inner surfaces of the upper screen reinforcement structure and the lower screen reinforcement structure, and the upper screen reinforcement structure includes several reinforcement Ring rib 201, several reinforcement longitudinal ribs 202, two end flanges 203, two longitudinal flanges 204 and reinforcement orifice plate 205, the screen 11 is installed on the inner surface of the upper screen reinforcement structure, the screen 11 A reinforcing orifice plate 205 is installed on the outer periphery, and many small holes are distributed on the screen 11 and the reinforcing orifice plate 205. The outer periphery of the reinforcing orifice plate 205 is longitudinally installed with a number of reinforcement longitudinal ribs 202, and transversely installed with a number of reinforcement ring ribs 201 , End flanges 203 are installed at both ends of several of the reinforcing longitudinal ribs 202, and longitudinal flanges 204 are installed at both ends of several of the reinforcing ring ribs 201. The upper screen reinforcement structure and the lower screen reinforcement structure pass through the longitudinal direction. The flange 204 is fixedly connected.
所述加强孔板205紧贴筛网11的外表面。所述筛网11上小孔的孔径为2.5-3.5mm,网壁厚为2-4mm,孔间距为4-7mm。所述加强孔板205的厚度为5-15mm。所述加强孔板205上小孔的孔径为25-30mm,孔间距为35-40mm。The reinforcing orifice plate 205 is in close contact with the outer surface of the screen mesh 11 . The aperture of the small holes on the screen mesh 11 is 2.5-3.5mm, the mesh wall thickness is 2-4mm, and the hole spacing is 4-7mm. The thickness of the reinforcing orifice plate 205 is 5-15 mm. The diameter of the small holes on the reinforcing orifice plate 205 is 25-30mm, and the hole spacing is 35-40mm.
所述螺旋挤压推进杆15对物料施加高压挤出的水分通过筛网排出,在排出水分的同时筛网也要承受螺旋挤压推进杆15通过物料施加的压力,而现有技术的筛网结构没有足够的强度和刚度来抵抗这种压力,一方面不能很好的发挥分离水分的作用,另一方面因为总损坏不能很好的长时间工作。本发明为解决现有技术的筛网结构没有足够的强度和刚度来抵抗压力的问题,设计了一种应用于该高压固液分离设备的筛网加固框架20。The water extruded by the
所述应用于高压固液分离设备的筛网加固框架为圆筒形结构,紧贴二级筛网11的是开有密布的大孔的外加强圆筒结构,再外侧紧贴设置了若干条纵环向环肋。为拆卸和维护方便,二级筛网沿周向等分为两个半圆筒的二级筛网11,外加强圆筒结构等分为两个加强孔板205。The screen reinforcement frame applied to the high-pressure solid-liquid separation equipment is a cylindrical structure, and the outer reinforcement cylindrical structure with densely clothed large holes is close to the secondary screen 11, and several strips are closely arranged on the outside. Longitudinal annular rib. For convenience of disassembly and maintenance, the secondary screen is divided into two semi-cylindrical secondary screens 11 in the circumferential direction, and the outer reinforced cylindrical structure is equally divided into two reinforced orifice plates 205 .
本发明所述的螺旋推进式高压固液分离机的具体操作过程和工作原理为:The specific operation process and working principle of the screw-propelled high-pressure solid-liquid separator of the present invention are as follows:
驱动电机18带动减速机17旋转,减速机17带动螺旋挤压推进杆15转动,粪污混合物料由进料口1进入缓冲室3,过量的物料由溢流口2返回到粪污池,缓冲室3的物料进入进料区4然后通过螺旋挤压推进杆15向前推进到初步挤压区5,经初压后物料被推进至间隔区6,当物料推进到二次挤压区7时,因为二次挤压段的螺旋叶片的螺距较小物料推进的速度较慢,这样便使物料在间隔区6得到进一步压缩,得到70%左右含水率的物料,物料经二次挤压区7被以更大的挤压力推进到无叶片的出料区9,在轴端阻滞挡板8的作用下达到出料口10后被挤出,经二次挤压后,物料含水率下降到50~55%。整个挤压过程使含水率大于80%有机细碎物料经过一台设备的挤压脱水即可使其含水率降至50~55%,挤压过程流畅,能耗低。The drive motor 18 drives the reducer 17 to rotate, and the reducer 17 drives the screw
以上所述的具体实施例,对本发明的目的、技术方案和有益效果进行了进一步详细说明。所应理解的是,以上所述仅为本发明的具体实施例而已,并不用于限制本发明,还可以是上述各个实施方式记载的特征的合理组合,凡在本发明精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The specific embodiments described above further describe the purpose, technical solutions and beneficial effects of the present invention in detail. It should be understood that the above descriptions are only specific embodiments of the present invention, and are not intended to limit the present invention, and may also be a reasonable combination of the features recorded in the above-mentioned various embodiments, all within the spirit and principle of the present invention, Any modification, equivalent replacement, improvement, etc. made should be included within the protection scope of the present invention.
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