CN113798011B - Heparin sodium production is with dry reducing mechanism - Google Patents
Heparin sodium production is with dry reducing mechanism Download PDFInfo
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- CN113798011B CN113798011B CN202111115558.0A CN202111115558A CN113798011B CN 113798011 B CN113798011 B CN 113798011B CN 202111115558 A CN202111115558 A CN 202111115558A CN 113798011 B CN113798011 B CN 113798011B
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- 229920000669 heparin Polymers 0.000 title claims abstract description 51
- ZFGMDIBRIDKWMY-PASTXAENSA-N heparin Chemical compound CC(O)=N[C@@H]1[C@@H](O)[C@H](O)[C@@H](COS(O)(=O)=O)O[C@@H]1O[C@@H]1[C@@H](C(O)=O)O[C@@H](O[C@H]2[C@@H]([C@@H](OS(O)(=O)=O)[C@@H](O[C@@H]3[C@@H](OC(O)[C@H](OS(O)(=O)=O)[C@H]3O)C(O)=O)O[C@@H]2O)CS(O)(=O)=O)[C@H](O)[C@H]1O ZFGMDIBRIDKWMY-PASTXAENSA-N 0.000 title claims abstract description 50
- 229960001008 heparin sodium Drugs 0.000 title claims abstract description 47
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 19
- 230000007246 mechanism Effects 0.000 title claims description 6
- 238000001035 drying Methods 0.000 claims abstract description 62
- 238000004891 communication Methods 0.000 claims abstract description 19
- 238000005485 electric heating Methods 0.000 claims abstract description 14
- 238000000227 grinding Methods 0.000 claims description 22
- 238000009423 ventilation Methods 0.000 claims description 19
- 238000007664 blowing Methods 0.000 claims description 17
- 238000007873 sieving Methods 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 8
- 239000006185 dispersion Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 4
- 238000010298 pulverizing process Methods 0.000 claims 2
- 239000000463 material Substances 0.000 claims 1
- 239000000843 powder Substances 0.000 abstract description 9
- 238000012545 processing Methods 0.000 abstract description 5
- 238000013461 design Methods 0.000 abstract description 2
- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 6
- 238000009826 distribution Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000013022 venting Methods 0.000 description 2
- 102000008946 Fibrinogen Human genes 0.000 description 1
- 108010049003 Fibrinogen Proteins 0.000 description 1
- 229920002683 Glycosaminoglycan Polymers 0.000 description 1
- HTTJABKRGRZYRN-UHFFFAOYSA-N Heparin Chemical compound OC1C(NC(=O)C)C(O)OC(COS(O)(=O)=O)C1OC1C(OS(O)(=O)=O)C(O)C(OC2C(C(OS(O)(=O)=O)C(OC3C(C(O)C(O)C(O3)C(O)=O)OS(O)(=O)=O)C(CO)O2)NS(O)(=O)=O)C(C(O)=O)O1 HTTJABKRGRZYRN-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 208000007536 Thrombosis Diseases 0.000 description 1
- 206010047249 Venous thrombosis Diseases 0.000 description 1
- 230000003266 anti-allergic effect Effects 0.000 description 1
- 230000002429 anti-coagulating effect Effects 0.000 description 1
- 230000003110 anti-inflammatory effect Effects 0.000 description 1
- 239000003146 anticoagulant agent Substances 0.000 description 1
- 229940127219 anticoagulant drug Drugs 0.000 description 1
- 239000004019 antithrombin Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 230000008827 biological function Effects 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 229940012952 fibrinogen Drugs 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 229960002897 heparin Drugs 0.000 description 1
- 238000000338 in vitro Methods 0.000 description 1
- 210000004347 intestinal mucosa Anatomy 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 208000010110 spontaneous platelet aggregation Diseases 0.000 description 1
- 210000003437 trachea Anatomy 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 210000001835 viscera Anatomy 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C4/00—Crushing or disintegrating by roller mills
- B02C4/02—Crushing or disintegrating by roller mills with two or more rollers
- B02C4/08—Crushing or disintegrating by roller mills with two or more rollers with co-operating corrugated or toothed crushing-rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0011—Heating features
- B01D1/0017—Use of electrical or wave energy
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/14—Evaporating with heated gases or vapours or liquids in contact with the liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/10—Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone
- B02C23/12—Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone with return of oversize material to crushing or disintegrating zone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/16—Separating or sorting of material, associated with crushing or disintegrating with separator defining termination of crushing or disintegrating zone, e.g. screen denying egress of oversize material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/28—Moving screens not otherwise provided for, e.g. swinging, reciprocating, rocking, tilting or wobbling screens
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/42—Drive mechanisms, regulating or controlling devices, or balancing devices, specially adapted for screens
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto
- B08B9/08—Cleaning containers, e.g. tanks
- B08B9/087—Cleaning containers, e.g. tanks by methods involving the use of tools, e.g. brushes, scrapers
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
本发明公开了一种肝素钠生产用干燥粉碎装置,涉及肝素钠生产加工技术领域。包括浓缩箱、干燥箱、粉碎箱和底座,干燥箱上端两侧开设有蒸汽出口,干燥箱内部下端中央转动连接中空的离心柱,离心柱上端设置有离心盘,离心盘上方连接离心桶,离心盘上表面设置多个分散槽,离心桶上端与干燥箱顶部滑动连接,第一连通口与离心桶上端中央相连通,干燥箱内壁上设置一层电热层。本发明克服了现有技术的不足,设计合理,使用方便,能够有效对肝素钠溶液进行干燥粉碎,且干燥效率高,生产加工连续性好,所得肝素钠粉末产品稳定性高,便于大规模生产使用。
The invention discloses a dry crushing device for producing heparin sodium, and relates to the technical field of heparin sodium production and processing. It includes a concentration box, a drying box, a crushing box and a base. There are steam outlets on both sides of the upper end of the drying box. The center of the lower end inside the drying box is rotated and connected to a hollow centrifugal column. A plurality of dispersing grooves are arranged on the upper surface of the plate, the upper end of the centrifugal bucket is slidably connected with the top of the drying box, the first communication port is connected with the center of the upper end of the centrifugal bucket, and an electric heating layer is set on the inner wall of the drying box. The invention overcomes the shortcomings of the prior art, has reasonable design, is convenient to use, can effectively dry and pulverize the heparin sodium solution, has high drying efficiency, good production and processing continuity, and the obtained heparin sodium powder product has high stability and is convenient for large-scale production use.
Description
技术领域technical field
本发明涉及肝素钠生产加工技术领域,尤其涉及一种肝素钠生产用干燥粉碎装置。The invention relates to the technical field of heparin sodium production and processing, in particular to a dry crushing device for heparin sodium production.
背景技术Background technique
肝素钠是从动物内脏中提取的一种硫酸氨基葡聚糖的钠盐,属粘多糖类物质,通过和抗凝血酶的结合产生抗凝血功能。临床研究表明,肝素钠除具有抗凝血作用外,还具有其他多种生物活性和临床用途,治疗急性静脉血栓和急性冠脉综合征、心绞痛、心肌梗塞、抗血栓、降血脂,可抑制体内体外动静脉血栓的形成,而又不影响血小板聚集和纤维蛋白原与血小板的结合,还可用于减少癌症相关的静脉血栓的复发。此外,肝素钠还具有抗炎、抗过敏等生物学功能。Heparin sodium is a sodium salt of aminodextran sulfate extracted from animal viscera, which belongs to mucopolysaccharides, and produces anticoagulant function by combining with antithrombin. Clinical studies have shown that in addition to its anticoagulant effect, heparin sodium also has a variety of other biological activities and clinical applications. In vitro arteriovenous thrombosis, without affecting platelet aggregation and fibrinogen binding to platelets, may also be used to reduce the recurrence of cancer-associated venous thrombosis. In addition, heparin sodium also has biological functions such as anti-inflammatory and anti-allergic.
一般肝素钠的制取大多是从猪小肠黏膜中提取,在提取过程中通常需要采用多种溶剂,获得提取液,最终再对提取液进行干燥后对干燥的产物进行粉碎处理,收集肝素钠成品粉末,由于肝素钠耐热性较好,现有的干燥方式大多直接采用高温干燥,但是由于提取液中液体含量较高,直接高温干燥效率较低,且后期粉碎处理需要转移装置进行处理,产品生产连续性差,降低实际生产的效率。Generally, the preparation of heparin sodium is mostly extracted from the pig small intestinal mucosa. During the extraction process, it is usually necessary to use a variety of solvents to obtain the extract. Finally, the extract is dried and the dried product is crushed to collect the finished product of heparin sodium. Powder, due to the good heat resistance of heparin sodium, most of the existing drying methods directly adopt high-temperature drying, but due to the high liquid content in the extract, the efficiency of direct high-temperature drying is low, and the later crushing treatment requires a transfer device for processing, the product Poor production continuity reduces the efficiency of actual production.
发明内容Contents of the invention
本发明的目的是为了解决现有技术中肝素钠干燥粉碎效率低,操作繁琐的问题,而提出的一种肝素钠生产用干燥粉碎装置。The purpose of the present invention is to solve the problems of low drying and crushing efficiency of heparin sodium and cumbersome operation in the prior art, and propose a dry crushing device for heparin sodium production.
为了实现上述目的,本发明采用了如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
一种肝素钠生产用干燥粉碎装置,包括依次连通的浓缩箱、干燥箱和粉碎箱,以及干燥箱底部设置有底座,所述浓缩箱底部中央设置第一连通口与干燥箱相连通,所述干燥箱上端两侧开设有蒸汽出口,所述干燥箱底部一侧设置有第二连通口与粉碎箱上端一侧相连通,所述干燥箱内部下端中央转动连接中空的离心柱,所述底座内部设置有离心电机,所述离心电机输出轴延伸至干燥箱内部,且离心电机输出轴通过转动皮带与离心柱相连接,所述离心柱上端设置有离心盘,且离心盘上方中央连接有侧壁呈镂空状的离心桶,所述离心盘上表面自中央向四周设置有多个分散槽,所述离心桶上端与干燥箱顶部滑动连接,所述第一连通口与离心桶上端中央相连通,所述离心桶内部设置有第一通气管,所述离心桶外部中段设置有一圈环形通气管,所述环形通气管两侧下端对称连通有第二通气管,所述第一通气管下端穿过离心盘且与离心盘转动连接,所述第一通气管和第二通气管底端穿过干燥箱延伸至底座内部与热风机相连通,所述第一通气管四周设置多个第一鼓气口,环形通气管靠近离心桶一侧设置多个第二鼓气口,所述干燥箱内壁上设置一层电热层。A dry crushing device for the production of heparin sodium, comprising a concentration box, a drying box and a crushing box connected in sequence, and a base is provided at the bottom of the drying box, and a first communication port is provided in the center of the bottom of the concentration box to communicate with the drying box. There are steam outlets on both sides of the upper end of the drying box, and a second communication port is provided on the bottom side of the drying box to communicate with the upper side of the crushing box. A centrifugal motor is provided, and the output shaft of the centrifugal motor extends to the inside of the drying box, and the output shaft of the centrifugal motor is connected with the centrifugal column through a rotating belt. The upper end of the centrifugal column is provided with a centrifugal disc, and the center of the centrifugal disc is connected with a side wall A hollow centrifugal bucket, the upper surface of the centrifugal disc is provided with a plurality of dispersion grooves from the center to the surroundings, the upper end of the centrifugal bucket is slidably connected to the top of the drying box, the first communication port is connected to the center of the upper end of the centrifugal bucket, The inside of the centrifuge barrel is provided with a first air pipe, and the outer middle section of the centrifugal bucket is provided with a ring-shaped air pipe. The lower ends of both sides of the annular air pipe are symmetrically connected with second air pipes. The centrifugal disc is rotatably connected with the centrifugal disc. The bottom ends of the first ventilation pipe and the second ventilation pipe pass through the drying box and extend to the inside of the base to communicate with the hot air blower. A plurality of first blowing ports are arranged around the first ventilation pipe , a plurality of second blowing ports are provided on the side of the annular ventilation pipe close to the centrifuge barrel, and a layer of electric heating layer is provided on the inner wall of the drying box.
优选的,所述干燥箱内壁上滑动连接有一圈环形刮板,所述干燥箱顶端两侧对称设置有气缸,所述气缸通过伸缩杆与环形刮板上端相连接。Preferably, a ring-shaped scraper is slidably connected to the inner wall of the drying box, and cylinders are arranged symmetrically on both sides of the top of the drying box, and the cylinder is connected to the upper end of the ring-shaped scraper through a telescopic rod.
优选的,所述蒸汽出口内部设置有抽气扇,所述抽气扇下端设置有一层过滤网层。Preferably, an exhaust fan is provided inside the steam outlet, and a filter layer is provided at the lower end of the exhaust fan.
优选的,所述第一鼓气口倾斜向下设置,所述第二鼓气口向一侧下方倾斜设置,所述第一通气管顶端设置有自中央向四周下方倾斜的倾斜板。Preferably, the first air blowing port is arranged obliquely downward, the second air blowing port is arranged obliquely downward to one side, and the top of the first ventilation pipe is provided with an inclined plate inclined downward from the center to the surrounding.
优选的,所述离心盘四周呈向上倾斜的弯折状。Preferably, the periphery of the centrifugal disc is bent upwards.
优选的,所述浓缩箱顶端一侧设置有第一进料口,所述浓缩箱顶端上方中央设置有搅拌电机,所述搅拌电机与浓缩箱内部设置的第一转轴相连接,所述第一转轴四周设置有电热板,所述第一连通口处设置有分液机构与干燥箱相连通。Preferably, a first feeding port is provided on one side of the top of the concentration box, and a stirring motor is provided in the center above the top of the concentration box, and the stirring motor is connected to a first rotating shaft provided inside the concentration box, and the first Electric heating plates are arranged around the rotating shaft, and a liquid separation mechanism is arranged at the first communication port to communicate with the drying box.
优选的,所述分液机构包括第一连通口内部转动连接的第二转轴和第二转轴四周设置的分料叶,所述分料叶与第一连通口内壁滑动连接,所述第二转轴与浓缩箱外部的分料电机相连接。Preferably, the liquid distributing mechanism includes a second rotating shaft that is rotatably connected inside the first communication port and a distributing leaf arranged around the second rotating shaft, the distributing leaf is slidably connected with the inner wall of the first communicating port, and the second rotating shaft It is connected with the distribution motor outside the enrichment tank.
优选的,所述粉碎箱一侧上端设置有第二进料口,所述粉碎箱内部中央侧壁上设置有一圈研磨层,所述研磨层中央设置有三个呈倒三角排布的研磨辊,所述粉碎箱底部一侧设置有第二出料口。Preferably, the upper end of one side of the crushing box is provided with a second feeding port, and a circle of grinding layer is provided on the inner central side wall of the crushing box, and three grinding rollers arranged in an inverted triangle are arranged in the center of the grinding layer, A second outlet is provided on one side of the bottom of the crushing box.
优选的,所述研磨辊下方设置有一层筛分网层,所述筛分网层呈倾斜状,且筛分网层倾斜低端的一侧壁设置有第一出料口,所述筛分网层底部设置有震动器。Preferably, a layer of sieving mesh layer is arranged under the grinding roller, the sieving mesh layer is inclined, and the side wall of the inclined lower end of the sieving mesh layer is provided with a first discharge port, and the sieving mesh layer is inclined. A vibrator is arranged at the bottom of the mesh layer.
优选的,所述研磨辊内部设置一层加热层。Preferably, a heating layer is arranged inside the grinding roller.
与现有技术相比,本发明提供了一种肝素钠生产用干燥粉碎装置,具备以下有益效果:Compared with the prior art, the present invention provides a dry crushing device for the production of heparin sodium, which has the following beneficial effects:
1、通过干燥箱中离心桶、离心盘、离心柱、转动皮带、第一通气管、第一鼓气口、第二通气管、环形通气管、第二鼓气口、电热层的设置,能够对肝素钠溶液进行高温离心处理,将溶液离心甩出,在通过热风鼓吹使其中溶剂成分快速蒸发,肝素钠固体颗粒随着向下的热风进入干燥箱底部,提升肝素钠干燥的效率;1. Through the setting of the centrifugal barrel, centrifugal disc, centrifugal column, rotating belt, first air pipe, first air blowing port, second air pipe, annular air pipe, second air blowing port and electric heating layer in the drying box, it can be used to heparin The sodium solution is subjected to high-temperature centrifugation, and the solution is centrifugally thrown out, and the solvent component is quickly evaporated by blowing hot air, and the solid particles of heparin sodium enter the bottom of the drying box with the downward hot air, improving the drying efficiency of heparin sodium;
2、通过浓缩箱中搅拌电机、第一转轴、电热板、第一连通口、第二转轴、分料叶的设置,能够有效将肝素钠提取液进行初步的蒸发浓缩,并且控制浓缩后肝素钠下落速度,方便控制后期离心时甩出的液滴密度,提升干燥的效率,同时保证所得的肝素钠呈分散的粉末状,方便后期研磨;2. Through the setting of the stirring motor, the first rotating shaft, the electric heating plate, the first connecting port, the second rotating shaft and the distributing leaf in the concentration box, the heparin sodium extract can be effectively evaporated and concentrated, and the heparin sodium after concentration can be controlled. The falling speed is convenient to control the density of the droplets thrown out during centrifugation in the later stage, improving the drying efficiency, and at the same time ensuring that the obtained heparin sodium is in the form of dispersed powder, which is convenient for later grinding;
3、通过粉碎箱中研磨层、研磨辊、加热层、筛分网层、第一出料口、第二出料口、震动器的设置,能够有效将干燥后的肝素钠进行研磨粉碎,提升肝素钠的细度,并且通过筛分网层进行筛分,将未达标的继续研磨,保证所得肝素钠产品的稳定性。3. Through the setting of the grinding layer, grinding roller, heating layer, sieving mesh layer, first discharge port, second discharge port and vibrator in the crushing box, the dried heparin sodium can be effectively ground and pulverized to improve The fineness of the heparin sodium is checked and sieved through the sieve mesh layer, and the unqualified ones are continued to be ground to ensure the stability of the obtained heparin sodium product.
该装置中未涉及部分均与现有技术相同或可采用现有技术加以实现,本发明设计合理,使用方便,能够有效对肝素钠溶液进行干燥粉碎,且干燥效率高,生产加工连续性好,所得肝素钠粉末产品稳定性高,便于大规模生产使用。The parts not involved in the device are the same as the prior art or can be realized by using the prior art. The present invention is reasonable in design, easy to use, can effectively dry and pulverize the heparin sodium solution, has high drying efficiency, and has good production and processing continuity. The obtained heparin sodium powder product has high stability and is convenient for large-scale production and use.
附图说明Description of drawings
图1为本发明正视剖面结构示意图;Fig. 1 is the schematic diagram of the front view sectional structure of the present invention;
图2为本发明侧视剖面结构示意图;Fig. 2 is a side view sectional structure schematic diagram of the present invention;
图3为本发明干燥箱正视剖面结构示意图;Fig. 3 is the schematic diagram of the front section structure of the drying oven of the present invention;
图4为本发明干燥箱俯视剖面结构示意图;Fig. 4 is a schematic diagram of a top view sectional structure of a drying oven of the present invention;
图5为本发明浓缩箱正视剖面结构示意图;Fig. 5 is a schematic diagram of the front view section structure of the concentration box of the present invention;
图6为本发明粉碎箱正视剖面结构示意图。Fig. 6 is a front view sectional structure diagram of a crushing box of the present invention.
图中:1、干燥箱;2、浓缩箱;3、粉碎箱;4、底座;5、热风机;6、离心电机;7、第一进料口;8、搅拌电机;9、第一转轴;10、电热板;11、第一连通口;12、第二转轴;13、分料叶;14、离心桶;15、离心盘;16、离心柱;17、转动皮带;18、第一通气管;19、第一鼓气口;20、第二通气管;21、环形通气管;22、第二鼓气口;23、电热层;24、环形刮板;25、气缸;26、伸缩杆;27、蒸汽出口;28、抽气扇;29、过滤网层;30、倾斜板;31、第二连通口;32、第二进料口;33、研磨层;34、研磨辊;35、加热层;36、筛分网层;37第一出料口;38、第二出料口;39、分料电机;40、分散槽;41、震动器。In the figure: 1. Drying box; 2. Concentration box; 3. Crushing box; 4. Base; 5. Hot air blower; 6. Centrifugal motor; 7. First feed port; ; 10, electric heating plate; 11, the first communication port; 12, the second rotating shaft; 13, the distribution leaf; 14, the centrifugal barrel; 15, the centrifugal disc; 16, the centrifugal column; 17, the rotating belt; Trachea; 19, the first blowing port; 20, the second venting pipe; 21, the annular venting pipe; 22, the second blowing port; 23, the electric heating layer; 24, the ring scraper; 25, the cylinder; 26, the expansion rod; 27 , steam outlet; 28, exhaust fan; 29, filter layer; 30, inclined plate; 31, second communication port; 32, second feed port; 33, grinding layer; 34, grinding roller; 35, heating layer ; 36, screen mesh layer; 37 first outlet; 38, second outlet; 39, distribution motor; 40, dispersion tank; 41, vibrator.
具体实施方式detailed description
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention.
在本发明的描述中,需要理解的是,术语“上”、“下”、“前”、“后”、“左”、“右”、“顶”、“底”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。In describing the present invention, it should be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", " The orientation or positional relationship indicated by "outside", etc. is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, so as to Specific orientation configurations and operations, therefore, are not to be construed as limitations on the invention.
实施例1:Example 1:
参照图1-6,一种肝素钠生产用干燥粉碎装置,包括依次连通的浓缩箱2、干燥箱1和粉碎箱3,以及干燥箱1底部设置有底座4,所述浓缩箱2底部中央设置第一连通口11与干燥箱1相连通,所述干燥箱1上端两侧开设有蒸汽出口27,所述干燥箱1底部一侧设置有第二连通口31与粉碎箱3上端一侧相连通,所述干燥箱1内部下端中央转动连接中空的离心柱16,所述底座4内部设置有离心电机6,所述离心电机6输出轴延伸至干燥箱1内部,且离心电机6输出轴通过转动皮带17与离心柱16相连接,所述离心柱16上端设置有离心盘15,且离心盘15上方中央连接有侧壁呈镂空状的离心桶14,所述离心盘15上表面自中央向四周设置有多个分散槽40,所述离心桶14上端与干燥箱1顶部滑动连接,所述第一连通口11与离心桶14上端中央相连通,所述离心桶14内部设置有第一通气管18,所述离心桶14外部中段设置有一圈环形通气管21,所述环形通气管21两侧下端对称连通有第二通气管20,所述第一通气管18下端穿过离心盘15且与离心盘15转动连接,所述第一通气管18和第二通气管20底端穿过干燥箱1延伸至底座4内部与热风机5相连通,所述第一通气管18四周设置多个第一鼓气口19,环形通气管21靠近离心桶14一侧设置多个第二鼓气口22,所述干燥箱1内壁上设置一层电热层23。Referring to Figures 1-6, a dry crushing device for heparin sodium production includes a
能够通过离心盘15和离心桶14对下落的溶液进行离心高速甩出,提升溶液与热空气的接触面积,提升干燥效率。The falling solution can be centrifugally thrown out at a high speed through the
实施例2:Example 2:
参照图1-6,本实施例与实施例1基本相同,优选的,所述干燥箱1内壁上滑动连接有一圈环形刮板24,所述干燥箱1顶端两侧对称设置有气缸25,所述气缸25通过伸缩杆26与环形刮板24上端相连接。能够有效将粘结在干燥箱1侧壁上的肝素钠粉末刮落,方便收集。Referring to Figures 1-6, this embodiment is basically the same as
为了方便蒸汽快速溢出,优选的,所述蒸汽出口27内部设置有抽气扇28,所述抽气扇28下端设置有一层过滤网层29。In order to facilitate the rapid overflow of steam, preferably, an
为了使肝素钠固体落入下方,便于收集,优选的,所述第一鼓气口19倾斜向下设置,所述第二鼓气口22向一侧下方倾斜设置,同时为了方便溶液在落入离心桶14中时,快速与离心桶14壁接触后被离心甩出,所述第一通气管18顶端设置有自中央向四周下方倾斜的倾斜板30。In order to make the heparin sodium solids fall below, it is convenient to collect, preferably, the first
为了控制离心盘15对液体离心甩出的方向,优选的,所述离心盘15四周呈向上倾斜的弯折状。In order to control the direction in which the
实施例3:Example 3:
参照图5,本实施例与实施例1基本相同,优选的,所述浓缩箱2顶端一侧设置有第一进料口7,所述浓缩箱2顶端上方中央设置有搅拌电机8,所述搅拌电机8与浓缩箱2内部设置的第一转轴9相连接,所述第一转轴9四周设置有电热板10,所述第一连通口11处设置有分液机构与干燥箱1相连通。有效对溶液进行初步浓缩,方便后期干燥处理。Referring to Fig. 5, this embodiment is basically the same as
为了控制溶液下落的速度,进一步控制容易而离心干燥的效果,优选的,所述分液机构包括第一连通口11内部转动连接的第二转轴12和第二转轴12四周设置的分料叶13,所述分料叶13与第一连通口11内壁滑动连接,所述第二转轴12与浓缩箱2外部的分料电机39相连接。In order to control the falling speed of the solution and further control the effect of easy and centrifugal drying, preferably, the liquid separation mechanism includes a second
实施例4:Example 4:
参照图6,本实施例与实施例1基本相同,优选的,所述粉碎箱3一侧上端设置有第二进料口32,所述粉碎箱3内部中央侧壁上设置有一圈研磨层33,所述研磨层33中央设置有三个呈倒三角排布的研磨辊34,所述粉碎箱3底部一侧设置有第二出料口38,能够有效对落入粉碎箱3中的肝素钠快速有效的粉碎,提升装置使用的连续性。Referring to Fig. 6, this embodiment is basically the same as
为了方便对肝素钠粉末进行筛分,控制肝素钠粉末的细度,优选的,所述研磨辊34下方设置有一层筛分网层36,所述筛分网层36呈倾斜状,且筛分网层36倾斜低端的一侧壁设置有第一出料口37,所述筛分网层36底部设置有震动器41。In order to sieve the heparin sodium powder conveniently and control the fineness of the heparin sodium powder, preferably, a
为了进一步保证肝素钠干燥的完成度,同时提升研磨的效率,优选的,所述研磨辊34内部设置一层加热层35。In order to further ensure the completeness of the drying of the heparin sodium and improve the grinding efficiency, preferably, a
工作原理:使用时,将肝素钠溶液加入浓缩箱2中,启动搅拌电机8对电热板10通电,使得肝素钠溶液进行搅拌加热浓缩,浓缩到一定程度后启动分料电机39和离心电机6,同时启动热风机5,并对电热层23进行通电加热,浓缩后的肝素钠溶液通过分料叶13缓慢的落入离心桶14中并通过倾斜板30靠近离心桶14侧壁后高速离心通过镂空位置甩出干燥,部分溶液落至离心盘15上,通过分散槽40离心甩出,甩出的液滴通过热风干燥和电热层23干燥后,启动抽气扇28,将蒸汽排出,干燥后的固体随热风的方向向下聚集后落入粉碎箱3中,且干燥过程中及时启动气缸25,通过环形刮板24刮除干燥箱1内壁上残留的肝素钠,肝素钠进入粉碎箱3中启动研磨辊34和震动器41,肝素钠经过研磨和筛分网层36筛分后,收集筛分后的粉末,将未通过筛分的继续研磨。Working principle: when in use, add the heparin sodium solution into the
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,根据本发明的技术方案及其发明构思加以等同替换或改变,都应涵盖在本发明的保护范围之内。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto, any person familiar with the technical field within the technical scope disclosed in the present invention, according to the technical solution of the present invention Any equivalent replacement or change of the inventive concepts thereof shall fall within the protection scope of the present invention.
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