CN103394638A - Method and apparatus for backwashing and regenerating casting used sand - Google Patents
Method and apparatus for backwashing and regenerating casting used sand Download PDFInfo
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- 239000004576 sand Substances 0.000 claims abstract description 220
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 84
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- 238000005406 washing Methods 0.000 claims abstract description 40
- 238000000034 method Methods 0.000 claims abstract description 39
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 230000001172 regenerating effect Effects 0.000 claims abstract description 13
- 238000011001 backwashing Methods 0.000 claims abstract description 12
- 230000009471 action Effects 0.000 claims abstract description 6
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 169
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 21
- 235000019353 potassium silicate Nutrition 0.000 description 15
- 238000005201 scrubbing Methods 0.000 description 7
- 239000004115 Sodium Silicate Substances 0.000 description 6
- 238000005265 energy consumption Methods 0.000 description 6
- 229910052911 sodium silicate Inorganic materials 0.000 description 6
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- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 3
- 229910001948 sodium oxide Inorganic materials 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
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- 229920001568 phenolic resin Polymers 0.000 description 2
- 239000005011 phenolic resin Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000009419 refurbishment Methods 0.000 description 2
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Abstract
一种逆洗再生铸造旧砂的方法与装置,借助摩擦和清洗进行脱膜,并通过旧砂和水流的相向运动实现水对旧砂的反复淋洗,使铸造旧砂连续再生。其装置由一根装有螺旋叶片的转轴和洗砂槽组成。转轴通过轴承安装在洗砂槽两端轴承座上,转轴一端的轴头与驱动装置相联,驱动装置一般是电动机和减速器。洗砂槽开有进砂口、出砂口及进水口、出液口。旧砂从进料斗加入,当转轴转动时,旧砂在螺旋叶片法向推力的轴向分力作用下,沿着洗砂槽轴向出液砂移动,从进水口来的清水在重力作用下向出液口运动,与砂形成逆向流动,对砂进行清洗,清洗干净的砂从出砂口排出,洗砂污水从出液口排出。为了提高清洗再生效果,可以采用热水和保温材料。
A method and device for backwashing and regenerating old foundry sand, which uses friction and cleaning to remove the film, and realizes repeated rinsing of the old sand by water through the opposite movement of the old sand and water flow, so that the used foundry sand can be continuously regenerated. The device consists of a rotating shaft equipped with spiral blades and a sand washing tank. The rotating shaft is installed on the bearing seats at both ends of the sand washing tank through bearings, and the shaft head at one end of the rotating shaft is connected with the driving device. The driving device is generally a motor and a reducer. The sand washing tank has a sand inlet, a sand outlet, a water inlet and a liquid outlet. The old sand is fed from the feeding hopper. When the rotating shaft rotates, the old sand moves along the axial direction of the sand washing tank under the action of the axial component force of the normal thrust of the spiral blade. It moves downward to the liquid outlet, forms a reverse flow with the sand, and cleans the sand. The cleaned sand is discharged from the sand outlet, and the sand washing sewage is discharged from the liquid outlet. In order to improve the cleaning and regeneration effect, hot water and thermal insulation materials can be used.
Description
技术领域 technical field
本发明涉及一种铸造旧砂的再生方法和装置。特别是一种逆洗式旧砂再生方法与装置,可以用于水玻璃旧砂、碱酚醛树脂旧砂和粘土旧砂的再生。 The invention relates to a method and device for regenerating used casting sand. In particular, a backwashing type used sand regeneration method and device can be used for regeneration of sodium silicate used sand, alkali phenolic resin used sand and clay used sand.
背景技术 Background technique
铸造旧砂再生的主要目是去除废旧砂粒上包裹着的残留粘结剂膜及杂物,恢复近于新砂的物理和化学性能,以重复使用。目前,除了干法再生和化学法再生外。铸造旧砂湿法再生脱膜效果特别好,再生砂的质量高,基本性能指标接近于新砂,可以作面砂使用,再生砂的回收率也很高(可达95%以上)。但以往的湿法再生系统结构较复杂庞大,耗水量大,湿法再生成本较高,污水量大,处理困难。降低湿法再生用水量和干燥能耗是应用湿法再生的关键。例如,对水玻璃旧砂进行湿式再生,可去除旧砂粒表面70%~90%的残留物,但用水量大,处理一吨砂耗水2~3吨,导致再生成本高,再生污水处理困难。由于运费攀升等因素的影响,新砂的价格有不断上升趋势;此外,随着土地减少和资源、环境压力不断增加,旧砂排放费不断上涨。在欧洲,再生费用已占到新砂购置费的85%~400%;所以,继续排放旧砂既浪费有限的硅砂资源,增加了成本,又污染了环境(包括碱污染及Pb、Ni、Cu、Hg等重金属污染)。可见,实现旧砂的再生和循环利用,已迫在眉睫。 The main purpose of the regeneration of old foundry sand is to remove the residual binder film and sundries wrapped on the used sand grains, and restore the physical and chemical properties close to new sand for repeated use. At present, in addition to dry regeneration and chemical regeneration. The wet regeneration and stripping effect of foundry old sand is particularly good. The quality of regenerated sand is high, and its basic performance indicators are close to that of new sand. It can be used as surface sand, and the recovery rate of regenerated sand is also high (up to 95%). However, the structure of the previous wet regeneration system is complex and large, the water consumption is large, the cost of wet regeneration is high, the amount of sewage is large, and the treatment is difficult. Reducing the water consumption and drying energy consumption of wet regeneration is the key to the application of wet regeneration. For example, wet regeneration of old sodium silicate sand can remove 70% to 90% of the residue on the surface of the old sand, but the water consumption is large, and the treatment of one ton of sand consumes 2 to 3 tons of water, resulting in high regeneration costs and difficult treatment of recycled sewage . Due to factors such as rising freight costs, the price of new sand has been on the rise; in addition, with land reduction and increasing pressure on resources and the environment, the discharge fee for old sand has continued to rise. In Europe, the cost of regeneration has accounted for 85% to 400% of the purchase cost of new sand; therefore, continuing to discharge old sand not only wastes limited silica sand resources, increases costs, but also pollutes the environment (including alkali pollution and Pb, Ni, Cu, Hg and other heavy metal pollution). It can be seen that it is imminent to realize the regeneration and recycling of old sand.
公开号CN1274627A和公开号 CN101209485A公开了一种热流旧砂再生机,主要由桶体、叶轮搅拌装置、加热装置、投药装置、机架等部分组成。桶体上部设有投药装置,桶体下部设有加热装置。由于机械搅拌、高温洗涤及化学药品的共同作用,以增加旧砂表面惰性膜在水中的脱落速度和溶解量,然后让污水透过再生砂层,并提出了搜集污水多次重复回用于清洗旧砂的构想。从而达到提高再生砂质量,减少污水产生之目的。 Publication No. CN1274627A and Publication No. CN101209485A disclose a heat flow old sand reclamation machine, which is mainly composed of a barrel body, an impeller stirring device, a heating device, a dosing device, a frame and the like. The upper part of the barrel body is provided with a dosing device, and the lower part of the barrel body is provided with a heating device. Due to the joint action of mechanical stirring, high-temperature washing and chemicals, to increase the shedding speed and dissolution amount of the inert film on the surface of the old sand in water, and then let the sewage pass through the regenerated sand layer, and propose to collect sewage repeatedly for cleaning Conception of old sand. So as to achieve the purpose of improving the quality of recycled sand and reducing the generation of sewage.
公开号CN2412680Y(专利200910060572.8)和公开号CN201423427Y(申请号CN200920083465)专利公开了一种浸泡渗漉的再生方法和装置。采用浸泡渗漉方法再将容器内的水玻璃砂振实后,向容器内加水,使水淹没砂的上表面,浸泡2-4小时后,打开容器底部的阀门将水缓慢排出;最后,把容器内的水玻璃砂放出、烘干即可再利用。这种水玻璃旧砂再生处理方法,用的水量少。但由于水玻璃旧砂形成的凝胶膜在常温态下难溶于水,凝胶膜包裹部分残留物并没有真正去除。所以,实际上达不到所宣称的效果,且处理时间长,再生效率低,实际应用难。 Publication No. CN2412680Y (Patent No. 200910060572.8) and Publication No. CN201423427Y (Application No. CN200920083465) disclose a regeneration method and device for immersion percolation. After vibrating the sodium silicate sand in the container by soaking and percolating, add water to the container to make the water submerge the upper surface of the sand. After soaking for 2-4 hours, open the valve at the bottom of the container to slowly discharge the water; finally, put The water glass sand in the container can be reused after being released and dried. The water glass old sand regeneration treatment method uses less water. But because the gel film formed by the old water glass sand is insoluble in water at normal temperature, the residue wrapped by the gel film has not been really removed. Therefore, in fact, the claimed effect cannot be achieved, and the treatment time is long, the regeneration efficiency is low, and the practical application is difficult.
专利200910310570.X提出了干法回收,湿法再生的构想,采用综合利用和面背砂造型工艺技术,使水玻璃旧砂再生。 Patent 200910310570.X proposes the idea of dry recovery and wet regeneration, and uses comprehensive utilization and face-back sand molding technology to regenerate the old water glass sand.
公开号CN102527929A(申请号201210012373.1)公开了一种水玻璃旧砂的蒸淋再生方法,向所述容器中破碎和筛分好的水玻璃旧砂通入100℃及以上高温水蒸汽对所述水玻璃旧砂进行蒸淋,能够有效清除水玻璃旧砂中的氧化钠,氧化钠含量低于0.25%,脱膜率达90%以上。处理过程用水量少,只有处理砂量的1/10~1/5。但该方法能耗较高,不利于推广应用。 Publication No. CN102527929A (Application No. 201210012373.1) discloses a method for regenerating old water glass sand by steaming and leaching. The broken and screened old water glass sand in the container is fed with high-temperature steam at 100°C or above to cool the water. The old glass sand is steamed, which can effectively remove the sodium oxide in the old water glass sand. The sodium oxide content is less than 0.25%, and the stripping rate is over 90%. The water consumption in the treatment process is less, only 1/10 to 1/5 of the amount of sand to be treated. But this method has high energy consumption, which is not conducive to popularization and application.
CN201210084186 公开号CN102615243A 公开了一种铸造旧砂湿法间歇式再生方法及其设备,该生方法包括一次擦洗步骤、二次擦洗步骤、三次擦洗步骤和检验步骤。再生设备包括搅拌机和砂水分离装置,搅拌机由支撑架、擦洗筒、驱动汽缸、电机和主轴构成,擦洗筒具有进砂口和进水口,并具有排水阀门和排砂阀门。该再生方法综合机械搅拌、清水洗涤和酸洗的共同作用,耗水量小、残留粘结剂去除率高、再生砂质量好;再生设备结构简单、能耗低、便于控制,容易实现自动化。但该方法采用间歇式再生方法,再生过程不能实现输送功能。 CN201210084186 Publication No. CN102615243A discloses a wet-process intermittent regeneration method and equipment for used foundry sand. The regeneration method includes a scrubbing step, a scrubbing step twice, a scrubbing step three times and an inspection step. The regeneration equipment includes a mixer and a sand-water separation device. The mixer is composed of a support frame, a scrubbing cylinder, a driving cylinder, a motor and a main shaft. The scrubbing cylinder has a sand inlet and a water inlet, and has a drain valve and a sand discharge valve. The regeneration method integrates the combined effects of mechanical stirring, clean water washing and pickling, has low water consumption, high removal rate of residual binder, and good quality of regenerated sand; the regeneration equipment has simple structure, low energy consumption, is easy to control, and is easy to realize automation. However, this method adopts an intermittent regeneration method, and the regeneration process cannot realize the conveying function.
CN201110056006 公开号CN102133616A提供了一种铸造混合废旧砂的再生回用方法,该方法首先将废旧砂分类、筛分、干燥去湿和干法再生,其次将适于湿法再生的再生砂进行湿法再生和脱水处理,将适于热法再生的再生砂进行热法再生,再次将两部分再生砂按照一定比例混合,利用热法再生砂的热量加热烘干湿法再生砂,最后经调湿、调温,得到再生回用砂。该方法有机结合了湿法再生工艺和热法再生工艺的优点,对混合废旧砂进行同步再生,避免了单一的湿法再生工艺的再生砂后期烘干的大能源消耗和单一的热法再生工艺的再生砂冷却时的热量浪费,降低了能源消耗和旧砂再生成本。 CN201110056006 Publication No. CN102133616A provides a recycling method for foundry mixed waste sand. In this method, the waste sand is first classified, screened, dried and dehumidified, and regenerated by dry method. Secondly, the regenerated sand suitable for wet regeneration is wet-processed. Regeneration and dehydration treatment, the regenerated sand suitable for thermal regeneration is regenerated by thermal method, and the two parts of regenerated sand are mixed again according to a certain ratio, and the heat of thermal regenerated sand is used to heat and dry the wet regenerated sand. Adjust the temperature to obtain recycled sand. This method organically combines the advantages of the wet regeneration process and the thermal regeneration process, and regenerates the mixed waste sand synchronously, avoiding the large energy consumption of the post-drying of the regenerated sand in the single wet regeneration process and the single thermal regeneration process The waste of heat during the cooling of regenerated sand reduces energy consumption and the cost of reclaiming old sand.
CN201010170597公开号CN101829759A和 CN201020188262 公开号CN201669371U公开了水玻璃旧砂回转振动研磨湿式再生机,包括钢螺旋橡胶复合弹簧、机架、外筒体、内筒体、筒体侧板、陶瓷磨球和振动电机,陶瓷磨球置于外筒体与内筒体之间形成的腔体内,所述振动电机有两只,两只振动电机一左一右固定连接于外筒体左右两边的机架上。该再生机采用回转振动研磨方法对水玻璃旧砂进行湿法再生,部件较多,结构相对复杂。 CN201010170597 Publication No. CN101829759A and CN201020188262 Publication No. CN201669371U disclose the rotary vibration grinding wet-type recycling machine of used water glass sand, including steel spiral rubber composite spring, frame, outer cylinder, inner cylinder, cylinder side plate, ceramic grinding ball and vibration The motor and the ceramic grinding ball are placed in the cavity formed between the outer cylinder and the inner cylinder. There are two vibration motors, one left and one right fixedly connected to the frame on the left and right sides of the outer cylinder. The recycling machine adopts the rotary vibration grinding method to regenerate the old water glass sand by wet method, and has many parts and relatively complex structure.
公开(公告)号CN103056291A发明公开了一种水玻璃旧砂热湿法-干法联合再生的方法。将水玻璃旧砂振动破碎,除去杂质后,高温水洗,去除沙粒表面的粘结剂膜;将水洗之后的水玻璃颗粒以300-350℃的高温烘干,实施干法再生,除去旧砂中的氧化钠、粉尘以及残余的烧结物。该联合湿法-干法再生方法过程复杂,能耗高。 Publication (announcement) No. CN103056291A invention discloses a combined regeneration method of hot-wet-dry method for used water glass sand. The old water glass sand is vibrated and crushed to remove impurities, then washed with high temperature water to remove the adhesive film on the surface of the sand grains; the water glass particles after washing are dried at a high temperature of 300-350°C, and dry regeneration is carried out to remove the old sand Sodium oxide, dust and residual sintered matter. The combined wet-dry regeneration method has complicated process and high energy consumption.
公开(公告)号CN102756073A发明涉及一种水玻璃旧砂翻新的设备,采用破碎设备、筛分设备、剥离设备、分级设备进行水玻璃旧砂再生,包括进料装置,该翻新设备还包括细碎机、筛分机、剥离机、分级机、带式收尘器,所述的进料装置与细碎机对接,该细碎机通过斗式提升机与筛分机连通,筛分机与溜槽连通,筛分机同时又与剥离机连通,该剥离机与分级机连通,分级机底部设置有重力式锁风卸料阀,所述的分级机又与带式收尘器连通,该生产工艺比较传统的湿法水洗翻新的生产工艺有占地面积小、受气候影响也小,同时也没有造成对水源的污染。比较另一种先进的水玻璃旧砂干法翻新的生产工艺有工艺流程简单、投资少、占地面积少的优点。 Publication (Announcement) No. CN102756073A invention relates to a kind of equipment for refurbishing old water glass sand, which uses crushing equipment, screening equipment, stripping equipment, and grading equipment to regenerate old water glass sand, including a feeding device. The refurbishment equipment also includes a fine crusher , a screening machine, a peeling machine, a classifier, a belt dust collector, the feeding device is connected to a fine crusher, the fine crusher is connected to the screening machine through a bucket elevator, the screening machine is connected to the chute, and the screening machine is simultaneously It is connected with the peeling machine, which is connected with the classifier. The bottom of the classifier is equipped with a gravity lock air discharge valve, and the classifier is connected with the belt dust collector. This production process is more traditional wet washing renovation The advanced production process has a small footprint, is less affected by the climate, and does not cause pollution to water sources. Compared with another advanced production process of dry refurbishment of old sodium silicate sand, it has the advantages of simple process flow, less investment and less floor space.
CN101780521A公开了一种强擦洗水玻璃旧砂湿法再生工艺,其主要特征是:磁选后的砂粒先后经过一级螺旋砂水分离器、一级湿法再生机和二级螺旋砂水分离器对旧砂进行砂水分离;再经过中和沉淀池对分离后的砂再进行中和;再经过二级湿法再生机、三级螺旋砂水分离器进行二次砂水分离,保证旧砂中存在的水玻璃能彻底去除干净;但步骤繁复,设备复杂。 CN101780521A discloses a wet regeneration process for strong scrubbing sodium silicate old sand. Its main features are: the sand particles after magnetic separation pass through the first-stage spiral sand-water separator, the first-stage wet regeneration machine and the second-stage spiral sand-water separator. Separation of sand and water for the old sand; then neutralize the separated sand through the neutralization sedimentation tank; and then carry out secondary sand-water separation through the secondary wet regenerator and the three-stage spiral sand-water separator to ensure that the old sand The water glass existing in it can be completely removed; but the steps are complicated and the equipment is complicated.
发明内容 Contents of the invention
本发明提出一种铸造旧砂逆洗再生方法,以减少铸造旧砂湿法再生用水量,并实现再生砂的输送,以达到旧砂充分利用及绿色环保的效果;同时提供用于该方法的设备,解决现有再生设备结构较复杂的问题,用于粘土旧砂、碱酚醛树脂旧砂和水玻璃旧砂的湿法再生。再生方法和再生装置主要有以下特征。 The present invention proposes a backwash regeneration method for old foundry sand to reduce the water consumption of wet regenerated old foundry sand and realize the transportation of regenerated sand so as to achieve the effect of full utilization of old sand and environmental protection; at the same time, it provides the method for The equipment solves the problem of complex structure of the existing regeneration equipment, and is used for the wet regeneration of clay old sand, alkali phenolic resin old sand and sodium silicate old sand. The regeneration method and regeneration device mainly have the following features.
1、本发明提及的再生方法借助擦洗作用脱膜,并通过旧砂和水流的相向运动实现水对旧砂的反复淋洗作用,达到铸造旧砂连续再生,再生方法工艺和设备简单易行、使用范围广。 1. The regeneration method mentioned in the present invention removes the film by means of scrubbing, and realizes the repeated leaching effect of water on the old sand through the relative movement of the old sand and the water flow, so as to achieve continuous regeneration of the old casting sand. The regeneration method process and equipment are simple and easy , A wide range of applications.
2、逆洗再生铸造旧砂装置的进砂口和清水进水口分别处于再生机的两端,旧砂在再生机的推动下朝出砂口运动;进水口的水压大于出水口的水压,从进水口进入的清水在压力或重力作用下朝出液口与旧砂相向运动,实现水对旧砂的反复淋洗作用。 2. The sand inlet and clean water inlet of the used sand device for backwashing regenerative casting are respectively located at both ends of the regenerator, and the old sand moves toward the sand outlet under the push of the recycler; the water pressure of the water inlet is greater than the water pressure of the water outlet , the clean water entering from the water inlet moves towards the liquid outlet and the old sand under the action of pressure or gravity, so as to realize the repeated washing effect of water on the old sand.
3、旧砂再生装置主要由一根装有螺旋叶片的转轴和洗砂槽组成。转轴通过轴承安装在料槽两端轴承座上,转轴一端的轴头与驱动装置相联,驱动装置一般是电动机和减速器。洗砂槽开有进、出砂口及进水口、出液口。逆洗再生铸造旧砂装置的清水进水口和出砂口留有一段距离,实现砂水分离,按到进砂口的距离计,与进水口比,出砂口远离进砂口,出砂口砂水分离后的湿砂从出砂口排出,再经脱水、烘干后,检验其质量合格后备用。 3. The used sand regeneration device is mainly composed of a rotating shaft equipped with spiral blades and a sand washing tank. The rotating shaft is installed on the bearing seats at both ends of the trough through bearings, and the shaft head at one end of the rotating shaft is connected with the driving device. The driving device is generally a motor and a reducer. The sand washing tank has an inlet and an outlet, a water inlet and a liquid outlet. There is a certain distance between the clean water inlet and the sand outlet of the backwash regeneration casting used sand device to realize the separation of sand and water. According to the distance to the sand inlet, compared with the water inlet, the sand outlet is far away from the sand inlet, and the sand outlet The wet sand after sand-water separation is discharged from the sand outlet, and after dehydration and drying, the quality is qualified before being used for later use.
4、旧砂再生过程如下:将砂斗中的旧砂从再生装置进砂口加入再生料槽,从再生机的进水口加入清水,开动再生机进行再生。当转轴转动时,物料受到螺旋叶片推力的作用,旧砂在叶片法向推力的轴向分力作用下,沿着料槽轴向出砂口移动,从进水口来的清水在重力作用下向出液口运动,与砂形成逆向流动,对砂进行清洗,最后,洗干净的砂从出砂口排出,洗砂污水从出液口排出。由于砂在排出之前,受到擦洗和清水的反复冲洗作用而更加清洁。 4. The old sand regeneration process is as follows: put the old sand in the sand hopper into the regeneration material tank from the sand inlet of the regeneration device, add clean water from the water inlet of the regeneration machine, and start the regeneration machine for regeneration. When the rotating shaft rotates, the material is affected by the thrust of the helical blade, and the old sand moves along the axial direction of the sand outlet of the trough under the action of the axial component of the normal thrust of the blade, and the clean water from the water inlet flows downward under the action of gravity The liquid outlet moves and forms a reverse flow with the sand to clean the sand. Finally, the cleaned sand is discharged from the sand outlet, and the sand washing sewage is discharged from the liquid outlet. The sand is cleaner because it is scrubbed and rinsed repeatedly with clean water before being discharged.
5、为了提高清洗再生效果,清洗水可以采用热水,可以在进水口安装热水装置,也可以另行安装热水锅炉,或者利用熔炼过程等冷却产生的热水,以节约能源。采用热水时,洗砂槽外包覆一层保温材料为佳。 5. In order to improve the cleaning and regeneration effect, hot water can be used for cleaning water, and a hot water device can be installed at the water inlet, or a hot water boiler can be installed separately, or the hot water generated by cooling in the smelting process can be used to save energy. When hot water is used, it is better to cover the sand washing tank with a layer of thermal insulation material.
6、根据再生砂质量的要求,可以通过加长再生装置工作部分的长度和调整螺旋转速等工作参数来实现。 6. According to the quality requirements of regenerated sand, it can be realized by lengthening the length of the working part of the reclaiming device and adjusting the working parameters such as the screw speed.
7、再生装置可以按一定角度安装,安装角度在0-90°之间。 7. The regeneration device can be installed at a certain angle, and the installation angle is between 0-90°.
逆洗再生铸造旧砂的方法与装置的特点如下。 The characteristics of the method and device for backwashing recycled foundry sand are as follows.
一、连续再生旧砂,再生后的旧砂砂粒均匀。 1. The old sand is continuously regenerated, and the regenerated old sand has uniform sand grains.
二、结构简单,操作维修方便。 2. Simple structure, convenient operation and maintenance.
三、体积小,造价低,制造材料易得。 3. The volume is small, the cost is low, and the manufacturing materials are easy to obtain.
四、在相同生产率条件下,比现有同类设备节水50-100%。 4. Under the same productivity conditions, it can save 50-100% of water compared with existing similar equipment.
五、可以在再生的同时实现输送,减少了动力消耗,节能50%。 5. It can realize transportation while regeneration, which reduces power consumption and saves energy by 50%.
六、可根据砂的种类和再生旧砂产量和脱膜率的不同要求,通过适当改变再生装备结构尺寸和工作参数来实现。 Sixth, it can be realized by appropriately changing the structure size and working parameters of the regeneration equipment according to the type of sand and the different requirements of the output and stripping rate of the regenerated old sand.
附图说明 Description of drawings
图1为本发明铸造旧砂再生装置总体结构示意图 Figure 1 is a schematic diagram of the overall structure of the foundry old sand regeneration device of the present invention
图中附图标记:l-槽体;2-螺旋轴;3-保温层;4-出砂口;5-轴承座;6-联轴器;7-驱动装置(电动机和减速器);8-进水口;9-进水阀;10-出液口;11-砂斗和进砂口;12-轴承座;13-轴承。 Reference signs in the figure: 1-tank body; 2-spiral shaft; 3-insulation layer; 4-sand outlet; 5-bearing seat; 6-coupling; 7-driving device (motor and reducer); 8 -water inlet; 9-water inlet valve; 10-liquid outlet; 11-sand bucket and sand inlet; 12-bearing seat; 13-bearing.
具体实施例 specific embodiment
旧砂再生装置的洗砂槽、进砂管、出砂管、螺旋轴、螺旋叶片、进水管、出液管均采用304不锈钢;保温材料采用玻璃纤维布。 The sand washing tank, sand inlet pipe, sand outlet pipe, screw shaft, spiral blade, water inlet pipe, and liquid outlet pipe of the used sand recycling device are all made of 304 stainless steel; the insulation material is made of glass fiber cloth.
实施例一,再生装置一洗砂槽与地面夹角为90°;洗砂槽、进砂管和出砂管外径均为100 mm,厚均为5 mm,长度分别为2000 mm、200 mm、1800 mm;螺旋轴直径20 mm,螺旋叶片直径88 mm;进砂管的弯头焊接在洗砂槽下端左侧,出砂管焊接在洗砂槽上端右侧,进砂口上用法兰联接进砂斗;进水管和出液管外径均为30 mm,厚为5 mm,进水管焊接在洗砂槽上端左侧,进水管与洗砂槽焊接处的上沿低于出砂管下沿10 mm;出液管焊接在进砂管上端左侧,出液管焊接处的上端低于进砂口10 mm;驱动装置采用无级调速电动机,功率为0.25-1.5 KW,转速范围40-200 rpm;保温层厚6 mm,实验数据见表1。 Embodiment 1, the angle between the sand washing tank and the ground of the regeneration device is 90°; the outer diameter of the sand washing tank, the sand inlet pipe and the sand outlet pipe are all 100 mm, the thickness is 5 mm, and the lengths are 2000 mm and 200 mm respectively , 1800 mm; the diameter of the screw shaft is 20 mm, and the diameter of the screw blade is 88 mm; the elbow of the sand inlet pipe is welded on the left side of the lower end of the sand washing tank, the sand outlet pipe is welded on the right side of the upper end of the sand washing tank, and the sand inlet is connected by a flange Sand bucket; the outer diameter of the water inlet pipe and the liquid outlet pipe is 30 mm, and the thickness is 5 mm. The water inlet pipe is welded on the left side of the upper end of the sand washing tank, and the upper edge of the weld between the water inlet pipe and the sand washing tank is lower than the lower edge of the sand outlet pipe 10 mm; the liquid outlet pipe is welded on the left side of the upper end of the sand inlet pipe, and the upper end of the liquid outlet pipe is 10 mm lower than the sand inlet; the driving device adopts a stepless speed regulating motor with a power of 0.25-1.5 KW and a speed range of 40- 200 rpm; the thickness of the insulation layer is 6 mm. The experimental data are shown in Table 1.
表1 实施例一的试验参数与效果 Table 1 Experimental parameters and effects of Example 1
实施例二,再生装置二的螺旋轴直径25 mm,螺旋叶片直径140 mm,洗砂槽与地面夹角45 °;洗砂槽、进砂管和出砂管外径分别为168 mm、150 mm、150 mm,厚均为10 mm,长度分别为2000 mm、150 mm、150 mm;进砂管和出砂管分别焊接在洗砂槽下端上方和上端下方,其中心分别离洗砂槽下端和上端各125 mm;进砂口上用法兰联接进砂斗。驱动电动机采用三相异步电动机,功率为5.5 KW,减速器采用R同轴式斜齿轮减速机,转速范围40-200 rpm;保温层厚10 mm,实验数据见表2。 Embodiment 2, the diameter of the screw shaft of regeneration device 2 is 25 mm, the diameter of the screw blade is 140 mm, the angle between the sand washing tank and the ground is 45 °; the outer diameters of the sand washing tank, sand inlet pipe and sand outlet pipe are 168 mm and 150 mm respectively , 150 mm, the thickness is 10 mm, and the lengths are 2000 mm, 150 mm, 150 mm respectively; the sand inlet pipe and the sand outlet pipe are respectively welded above the lower end of the sand washing tank and below the upper end, and their centers are respectively separated from the lower end of the sand washing tank and The upper ends are 125 mm each; the sand inlet is connected to the sand bucket with a flange. The driving motor is a three-phase asynchronous motor with a power of 5.5 KW. The reducer is an R coaxial helical gear reducer with a speed range of 40-200 rpm. The thickness of the insulation layer is 10 mm. The experimental data are shown in Table 2.
表2 实施例二的试验参数与效果 Table 2 Experimental parameters and effects of embodiment two
实施例三,旧砂再生装置三的洗砂槽与地面夹角0°;洗砂槽、进砂管和出砂管外径均为100 mm,厚均为5 mm,长度分别为2000 mm、200 mm、1800 mm;螺旋轴直径20 mm,螺旋叶片直径88 mm;进砂管焊接在洗砂槽左侧上端,出砂管的弯头焊接在洗砂槽右侧上端,出砂管的中轴线与洗砂槽中轴线为异面垂直关系;进砂口上用法兰联接进砂斗;进水管和出液管 的外径均为30 mm,厚为5 mm,进水管焊接在洗砂槽上端左侧,与洗砂槽焊接处的上沿低于出砂管下沿10 mm;出液管焊接在进砂管上端左侧,出液管焊接处的上端低于进砂口10 mm;驱动装置采用无级调速电动机,功率为0.25-1.5 KW,转速范围40-200 rpm;保温层厚6 mm,实验数据见表3。 Embodiment 3, the angle between the sand washing tank and the ground of the old sand regeneration device 3 is 0°; the outer diameter of the sand washing tank, the sand inlet pipe and the sand outlet pipe are all 100 mm, the thickness is 5 mm, and the lengths are respectively 2000 mm, 200 mm, 1800 mm; the diameter of the screw shaft is 20 mm, and the diameter of the screw blade is 88 mm; the sand inlet pipe is welded at the upper left end of the sand washing tank, the elbow of the sand outlet pipe is welded at the upper right end of the sand washing tank, and the middle of the sand outlet pipe The axis and the central axis of the sand washing tank are perpendicular to each other; the sand inlet is connected to the sand bucket with a flange; the outer diameter of the water inlet pipe and the liquid outlet pipe are both 30 mm and the thickness is 5 mm, and the water inlet pipe is welded on the upper end of the sand washing tank On the left side, the upper edge of the welding part with the sand washing tank is 10 mm lower than the lower edge of the sand outlet pipe; the liquid outlet pipe is welded on the left side of the upper end of the sand inlet pipe, and the upper end of the welding part of the liquid outlet pipe is 10 mm lower than the sand inlet; The device adopts a stepless speed regulating motor with a power of 0.25-1.5 KW and a speed range of 40-200 rpm; the thickness of the insulation layer is 6 mm. The experimental data are shown in Table 3.
表3 实施例三的试验参数与效果 Table 3 Experimental parameters and effects of Example three
最后所应说明的是,以上具体实施方式仅用以说明本发明的技术方案而非限制,尽管参照较佳实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范围,其均应涵盖在本发明的权利要求范围当中。 Finally, it should be noted that the above specific embodiments are only used to illustrate the technical solutions of the present invention and not limit them. Although the present invention has been described in detail with reference to preferred embodiments, those skilled in the art should understand that the present invention can be Modifications or equivalent replacements of the technical solutions without departing from the spirit and scope of the technical solutions of the present invention shall fall within the scope of the claims of the present invention.
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