WO2019128114A1 - Royal jelly filtration apparatus and method - Google Patents
Royal jelly filtration apparatus and method Download PDFInfo
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- WO2019128114A1 WO2019128114A1 PCT/CN2018/090283 CN2018090283W WO2019128114A1 WO 2019128114 A1 WO2019128114 A1 WO 2019128114A1 CN 2018090283 W CN2018090283 W CN 2018090283W WO 2019128114 A1 WO2019128114 A1 WO 2019128114A1
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- royal jelly
- chamber
- filter
- filtering
- liquid level
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- 238000001914 filtration Methods 0.000 title claims abstract description 153
- 229940109850 royal jelly Drugs 0.000 title claims abstract description 152
- 238000000034 method Methods 0.000 title claims abstract description 21
- 230000007246 mechanism Effects 0.000 claims abstract description 120
- 239000007788 liquid Substances 0.000 claims description 90
- 239000002002 slurry Substances 0.000 claims description 83
- 239000002893 slag Substances 0.000 claims description 75
- 238000003860 storage Methods 0.000 claims description 57
- 238000003756 stirring Methods 0.000 claims description 30
- 230000001105 regulatory effect Effects 0.000 claims description 16
- 230000009467 reduction Effects 0.000 claims description 9
- 238000000265 homogenisation Methods 0.000 claims description 7
- 238000013022 venting Methods 0.000 claims description 7
- 238000009413 insulation Methods 0.000 claims description 3
- 238000013019 agitation Methods 0.000 claims description 2
- 238000012544 monitoring process Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 12
- 238000000967 suction filtration Methods 0.000 abstract description 2
- 239000013049 sediment Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- 238000007790 scraping Methods 0.000 description 6
- QHBZHVUGQROELI-UHFFFAOYSA-N Royal Jelly acid Natural products OCCCCCCCC=CC(O)=O QHBZHVUGQROELI-UHFFFAOYSA-N 0.000 description 5
- 235000013871 bee wax Nutrition 0.000 description 5
- 239000012166 beeswax Substances 0.000 description 5
- 238000007872 degassing Methods 0.000 description 5
- 235000013305 food Nutrition 0.000 description 5
- 239000012535 impurity Substances 0.000 description 5
- KUPHXIFBKAORGY-UHFFFAOYSA-N 2-amino-3-iodo-4-methylbenzoic acid Chemical compound CC1=CC=C(C(O)=O)C(N)=C1I KUPHXIFBKAORGY-UHFFFAOYSA-N 0.000 description 4
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 230000002411 adverse Effects 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 235000004977 Brassica sinapistrum Nutrition 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 238000012840 feeding operation Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 239000002932 luster Substances 0.000 description 2
- QHBZHVUGQROELI-SOFGYWHQSA-N (E)-10-hydroxydec-2-enoic acid Chemical compound OCCCCCCC\C=C\C(O)=O QHBZHVUGQROELI-SOFGYWHQSA-N 0.000 description 1
- 235000014698 Brassica juncea var multisecta Nutrition 0.000 description 1
- 240000002791 Brassica napus Species 0.000 description 1
- 235000006008 Brassica napus var napus Nutrition 0.000 description 1
- 235000006618 Brassica rapa subsp oleifera Nutrition 0.000 description 1
- 244000188595 Brassica sinapistrum Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 241000208832 Viburnum Species 0.000 description 1
- 235000019013 Viburnum opulus Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000975 bioactive effect Effects 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- 239000005556 hormone Substances 0.000 description 1
- 230000010358 mechanical oscillation Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000010355 oscillation Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 102000004196 processed proteins & peptides Human genes 0.000 description 1
- 108090000765 processed proteins & peptides Proteins 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000006188 syrup Substances 0.000 description 1
- 235000020357 syrup Nutrition 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
- B01D29/03—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L21/00—Marmalades, jams, jellies or the like; Products from apiculture; Preparation or treatment thereof
- A23L21/20—Products from apiculture, e.g. royal jelly or pollen; Substitutes therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/60—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration
- B01D29/605—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration by level measuring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/62—Regenerating the filter material in the filter
- B01D29/64—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element
- B01D29/6407—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element brushes
- B01D29/6423—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element brushes with a translational movement with respect to the filtering element
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/001—Filters in combination with devices for the removal of gas, air purge systems
Definitions
- the invention relates to the technical field of bee product processing, in particular to a royal jelly filtering device and method.
- the filtering device has the advantages of simple structure and convenient operation, but has the following disadvantages: continuous filtration cannot be realized, and the royal jelly raw material needs to be continuously added in the production process; the efficiency in the initial stage of filtration is high, and in the middle and late stages, beeswax residue in the royal jelly, 10-HDA ( Royal jelly acid, crystals, bee corpses and other impurities can easily block the filter, so it is necessary to frequently replace and clean the filter, resulting in reduced production efficiency, more loss of royal jelly, low filtration efficiency; air squeeze filtration in filtration, filtration of royal jelly air Carrying a large amount causes oxidation of some biologically active ingredients.
- the object of the present invention is to provide a royal jelly filtration device and method, which solves the problem that the existing royal jelly filtration mode cannot achieve continuous filtration, easily clogging the filter mesh, has low filtration efficiency, and easily causes oxidative degradation of the biological active component.
- the present invention provides a royal jelly filtering device comprising a reciprocating filtering device and a venting slurry storage device connected to the reciprocating filtering device;
- the first driving mechanism includes an active mechanism and a driven mechanism disposed above the filter chamber, and the active mechanism and the driven mechanism are respectively disposed on the front and rear sides of the filter chamber;
- the active mechanism includes a lead screw, an active slider disposed on the lead screw, and a servo motor drivingly coupled to the lead screw;
- the driven mechanism includes a guide rod, and a guide rod disposed on the guide rod follow the slider.
- the reciprocating filter device further includes a first frame, the filter chamber is mounted on the first frame, and a mounting plate is disposed on the first frame, and the mounting plate is disposed at the Above the filter chamber, the active mechanism and the driven mechanism are both disposed on the mounting plate;
- the vented slurry storage device further includes a second frame, and the slurry chamber is disposed at the second On the rack.
- the evacuation venting mechanism includes an exhaust line connected to the slurry chamber and a vacuum pump connected to the exhaust line.
- the filter screen divides the filter chamber into an upper slag filter compartment and a lower slurry storage compartment
- the upper slag filter compartment is a rectangular tank structure
- the lower slurry storage compartment is a funnel-shaped structure, wherein
- the lower slurry storage compartment is connected to the slurry chamber through a slurry delivery line; a seal is provided at a junction between the upper slag filtration compartment and the lower slurry storage compartment, the filter Disposed on the gasket.
- a first liquid level sensor is disposed in the upper slag filtering sub-chamber
- a second liquid level sensor is disposed in the slurry storage chamber
- the slurry conveying pipeline is disposed at an outlet of the lower slurry storage sub-chamber
- a first control valve is disposed, and a second control valve is disposed on the slurry delivery line disposed at the inlet of the slurry chamber, and a third control valve is disposed on the exhaust line.
- the device further includes a control device including an automatic controller, the automatic controller and the servo motor, the reduction motor, the vacuum pump, the first liquid level sensor, the second liquid level sensor, and the first control The valve, the second control valve and the third control valve are connected.
- a control device including an automatic controller, the automatic controller and the servo motor, the reduction motor, the vacuum pump, the first liquid level sensor, the second liquid level sensor, and the first control The valve, the second control valve and the third control valve are connected.
- the invention also provides a method for filtering royal jelly, which adopts the above-mentioned royal jelly filtering device, and specifically comprises the following steps:
- the first control valve and the third control valve are opened, the vacuum pump is activated, and when the vacuum pressure meets the set requirement, the second control valve is opened to start the servo motor, and the slag removing mechanism Performing automatic filtration and slag removal operations, and monitoring the level of the royal jelly in the filtration chamber in real time by the first liquid level sensor;
- the royal jelly filtering device and method provided by the invention drive the stirring mechanism to move by the second driving mechanism, thereby realizing the homogenization and degassing operation of the royal jelly, and the vacuuming and exhausting is realized by the vacuuming and exhausting mechanism, and the filtration efficiency of the royal jelly is improved. It can realize low-temperature rapid filtration, and the filtered royal jelly is stored in a low-temperature, vacuum, dark-proof storage chamber, which effectively reduces the adverse effects of oxygen, light and temperature on the filtration of royal jelly.
- the royal jelly filtering device and method provided by the invention combines reciprocating slag and negative pressure suction filtering, and when the royal jelly in the filtering chamber is filtered, the royal jelly in the slurry chamber simultaneously completes degassing and homogenizing operation, which is not only greatly shortened The contact time between royal jelly and air is effective, and the total production time of royal jelly is effectively reduced.
- the royal jelly is in a low-oxygen state after being filtered into the slurry storage chamber. At the same time, by providing an insulation layer outside the slurry storage, the low-temperature storage condition is maintained, and the effect of the royal jelly is more effectively preserved. ingredient.
- the royal jelly filtering device and method provided by the invention adopts a pressure-adjustable slag removing mechanism, and the slag removing mechanism can automatically scrape the filter residue accumulated on the filter net during the reciprocating motion, and the filter residue can be temporarily stored on both sides of the filter net.
- the existing royal jelly filtration mode greatly reduces the possibility of secondary clogging of the filter slag, and greatly improves the filtration efficiency and stability.
- the royal jelly filtering device and method provided by the invention adopts an automatic controller to control the working of the first driving mechanism, the second driving mechanism, the vacuuming exhausting mechanism and the respective control valves, and simultaneously adopts the liquid level sensor to separately monitor the filtering chamber and the slurry.
- the indoor royal jelly liquid level not only has high control precision and high reliability, but also realizes automatic high-efficiency continuous filtration of royal jelly, which reduces production cost.
- FIG. 1 is a schematic structural view of a royal jelly filtering device according to an embodiment of the present invention.
- Figure 2 is an enlarged view of a portion A of Figure 1 of the royal jelly filtration device of the embodiment of the present invention
- FIG. 3 is a top plan view of a reciprocating filter device in a royal jelly filter device according to an embodiment of the present invention
- FIG. 4 is a schematic view of a stirring mechanism in a royal jelly filtration device according to an embodiment of the present invention.
- 1 filter chamber; 101: upper slag filter compartment; 102: lower slurry storage compartment; 2: filter; 3: slag removal mechanism; 301: pressure regulation plate; 302: support beam; 303: fixed seat; 304: slag scraping plate; 305: column; 306: spring; 307: adjusting bolt; 4: pulping chamber; 5: stirring mechanism; 6: geared motor; 7: screw; 8: active slider; Motor; 10: guide rod; 11: driven slider; 12: first frame; 13: mounting plate; 14: second frame; 15: exhaust pipe; 16: vacuum pump; 17: slurry conveying pipe 18: seal; 19: first level sensor; 20: second level sensor; 21: first control valve; 22: second control valve; 23: third control valve; 24: automatic controller; :Insulation.
- an embodiment of the present invention provides a royal jelly filtering device including a reciprocating filtering device and a venting slurry storage device connected to the reciprocating filtering device.
- the reciprocating filter device includes a filter chamber 1, a filter screen 2 disposed in the filter chamber 1, a slag removal mechanism 3 disposed on the filter screen 2, and a drive for the slag removal mechanism 3 at the filter A first drive mechanism for linear reciprocating motion on the net 2.
- the venting type slurry storage device includes a slurry storage chamber 4, a stirring mechanism 5 disposed in the slurry storage chamber 4, a second driving mechanism that drives the stirring mechanism 5 to perform a stirring operation, and a storage chamber 4 connected vacuum exhaust mechanism.
- the royal jelly filtering device drives the slag removal mechanism 3 to perform linear reciprocating motion on the filter net 2 by the first driving mechanism, thereby realizing continuous filtration production of royal jelly, thereby realizing automatic filtration operation of royal jelly. And standard work, which is conducive to the standardization of the royal jelly production process.
- the stirring mechanism is driven by the second driving mechanism to perform a stirring motion, and the vacuuming and exhausting mechanism is used to realize vacuuming and exhausting, thereby realizing homogenization and degassing operation of the royal jelly, and improving the filtration efficiency of the royal jelly.
- the royal jelly filtering device combines the reciprocating slag and the negative pressure suction filter.
- the royal jelly in the slurry storage chamber 4 is simultaneously removed. Gas and homogenization work not only greatly shortens the contact time between royal jelly and air, but also effectively reduces the total production time of royal jelly.
- the royal jelly is filtered into the slurry storage chamber 4, it is in a vacuum, low oxygen and dark state, thus effectively protecting the royal jelly. Functional ingredients.
- the first driving mechanism includes an active mechanism and a driven mechanism disposed above the filter chamber 1, and the active mechanism and the driven mechanism are respectively disposed on the front and rear sides of the filter chamber 1 respectively. .
- the active mechanism includes a lead screw 7, an active slider 8 disposed on the lead screw 7, and a servo motor 9 drivingly coupled to the lead screw 7, the servo motor 9 driving the lead screw 7
- the clockwise or counterclockwise rotation is performed to drive the active slider 8 to linearly reciprocate along the lead screw 7.
- the second drive mechanism includes a reduction motor 6 connected to the agitation mechanism 5.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Jellies, Jams, And Syrups (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Filtration Of Liquid (AREA)
Abstract
Provided are a royal jelly filtration apparatus and method. The filtration apparatus comprises a reciprocating filtration apparatus and an air-discharge jelly-storing apparatus. The reciprocating filtration apparatus comprises a filtration chamber (1), a filtration mesh (2), a sediment-removing mechanism (3), and a first drive mechanism. The air-discharge jelly-storing apparatus comprises a jelly-storing chamber (4), a mixing mechanism (5), a second drive mechanism, and a vacuumization and air-discharge mechanism. The first drive mechanism drives the sediment-removing mechanism (3) in linear reciprocating motion on the filtration mesh (2), thereby accomplishing continuous filtration and production of the royal jelly; by means of a combination of reciprocating sediment removal and negative-pressure suction filtration, the efficiency of filtration of royal jelly is increased.
Description
交叉引用cross reference
本申请引用于2017年12月27日提交的专利名称为“一种蜂王浆过滤装置及方法”的第2017114479532号中国专利申请,其通过引用被全部并入本申请。The present application is hereby incorporated by reference in its entirety in its entirety in its entirety in its entirety in the the the the the the the the the
本发明涉及蜂产品加工技术领域,尤其涉及一种蜂王浆过滤装置及方法。The invention relates to the technical field of bee product processing, in particular to a royal jelly filtering device and method.
蜂王浆生产加工过程中需要去除其含有的蜂尸体、蜂蜡渣和灰尘等杂质,因此需要进行过滤处理。新鲜蜂王浆呈乳浆状,为半流体,而且蜂王浆中存在的杂质和10-羟基-2-癸烯酸(10-HDA)结晶体很容易堵塞过滤网,因此蜂王浆过滤十分困难。新鲜蜂王浆含有丰富的活性肽、激素、酶类等丰富的生物活性物质,其生物活性不稳定,在温度、光照、空气、加工等条件影响下,易受到破坏,尤其是温度影响其保健功效。因此,提高过滤效率和质量,将有利于减少蜂王浆生物活性物质的降解,保持蜂王浆品质和新鲜度。During the production and processing of royal jelly, it is necessary to remove impurities such as bee carcasses, beeswax slag and dust, so it needs to be filtered. The fresh royal jelly is in the form of a syrup, which is semi-fluid, and the impurities present in the royal jelly and the 10-hydroxy-2-decenoic acid (10-HDA) crystals easily clog the filter, so the filtration of the royal jelly is very difficult. Fresh royal jelly is rich in active peptides, hormones, enzymes and other biologically active substances. Its biological activity is unstable, and it is easily damaged under the influence of temperature, light, air, processing and other conditions, especially the temperature affects its health care effect. Therefore, improving filtration efficiency and quality will help reduce the degradation of royal jelly bioactive substances and maintain the quality and freshness of royal jelly.
现有的蜂王浆的过滤方式主要有以下两种方法:一、通过活塞压缩空气来实现蜂王浆过滤。这种过滤方式装置结构简单,操作方便,但是存在如下缺点:无法实现连续过滤,生产过程中需要不断加入蜂王浆原料;过滤初始阶段效率较高,中后期由于蜂王浆中的蜂蜡渣、10-HDA(王浆酸)晶体、蜂尸体等杂质极易堵塞过滤网,因此需要经常更换、清洗过滤网,导致生产效率下降,蜂王浆损失较多,过滤效率低;过滤中采用空气挤压过滤,过滤所得蜂王浆空气携带量大,导致部分生物活性成分氧化。二、通过机械振荡过滤网来实现蜂王浆过滤。这种过滤方式机械结构相对简单,操作比较方便。但是存在如下缺点:过滤初始阶段效率较高,后期由于蜂王浆中的蜂蜡渣、10-HDA(王浆酸)晶体、蜂尸体等杂质极易堵塞 过滤网,导致过滤效率大大下降;装置虽然设置了除渣口,但是并没有设计配套装置来实现除渣功能,只通过振荡除渣,除渣效果较差,因此操作过程中还需要人工除渣或更换振荡筛网来提高过滤效率,难以实现高效连续过滤作业;过滤中采用振荡作业,振荡过程中加大了蜂王浆与空气接触的可能性,从而加剧了蜂王浆生物活性成分氧化劣变。There are two main methods for filtering the existing royal jelly: First, the royal jelly is filtered by the compressed air of the piston. The filtering device has the advantages of simple structure and convenient operation, but has the following disadvantages: continuous filtration cannot be realized, and the royal jelly raw material needs to be continuously added in the production process; the efficiency in the initial stage of filtration is high, and in the middle and late stages, beeswax residue in the royal jelly, 10-HDA ( Royal jelly acid, crystals, bee corpses and other impurities can easily block the filter, so it is necessary to frequently replace and clean the filter, resulting in reduced production efficiency, more loss of royal jelly, low filtration efficiency; air squeeze filtration in filtration, filtration of royal jelly air Carrying a large amount causes oxidation of some biologically active ingredients. Second, through the mechanical oscillation filter to achieve royal jelly filtration. The mechanical structure of the filtering method is relatively simple and the operation is convenient. However, there are the following disadvantages: the efficiency of the initial stage of filtration is high, and the impurities are greatly blocked due to impurities such as beeswax residue, 10-HDA (parent acid) crystals, and bee corpses in the royal jelly, which greatly reduces the filtration efficiency; Slag mouth, but there is no design equipment to achieve the slag removal function, only by oscillating slag, the slag removal effect is poor, so the operation process also needs manual slag removal or replacement of the oscillating screen to improve the filtration efficiency, it is difficult to achieve efficient continuous Filtration operation; oscillating operation is used in the filtration, and the possibility of contact of the royal jelly with the air is increased during the oscillation process, thereby aggravating the oxidative deterioration of the biological active component of the royal jelly.
发明内容Summary of the invention
(一)要解决的技术问题(1) Technical problems to be solved
本发明的目的是提供一种蜂王浆过滤装置及方法,解决现有蜂王浆过滤方式存在的无法实现连续过滤,易堵塞过滤网,过滤效率低,容易导致生物活性成分氧化劣变的问题。The object of the present invention is to provide a royal jelly filtration device and method, which solves the problem that the existing royal jelly filtration mode cannot achieve continuous filtration, easily clogging the filter mesh, has low filtration efficiency, and easily causes oxidative degradation of the biological active component.
(二)技术方案(2) Technical plan
为了解决上述技术问题,本发明提供了一种蜂王浆过滤装置,包括往复式过滤装置以及与所述往复式过滤装置相连的排气式储浆装置;In order to solve the above technical problems, the present invention provides a royal jelly filtering device comprising a reciprocating filtering device and a venting slurry storage device connected to the reciprocating filtering device;
其中,所述往复式过滤装置包括过滤室、设置在所述过滤室中的过滤网、设置在所述过滤网上的除渣机构、以及驱动所述除渣机构在所述过滤网上进行直线往复运动的第一驱动机构;Wherein the reciprocating filter device comprises a filter chamber, a filter mesh disposed in the filter chamber, a slag removing mechanism disposed on the filter mesh, and driving the slag removing mechanism to perform linear reciprocating motion on the filter mesh First drive mechanism;
所述排气式储浆装置包括储浆室、设置在所述储浆室中的搅拌机构、驱动所述搅拌机构进行搅拌动作的第二驱动机构、以及与所述储浆室相连的抽真空排气机构。The vented slurry storage device includes a slurry storage chamber, a stirring mechanism disposed in the slurry storage chamber, a second driving mechanism that drives the stirring mechanism to perform a stirring operation, and an evacuation vacuum connected to the slurry storage chamber Exhaust mechanism.
进一步地,所述第一驱动机构包括设置在所述过滤室上方的主动机构和从动机构,所述主动机构和所述从动机构分别对应设置在所述过滤室的前后两侧;其中,所述主动机构包括丝杆、设置在所述丝杠上的主动滑块、以及与所述丝杠驱动连接的伺服电机;所述从动机构包括导杆、以及设置在所述导杆上的从动滑块。Further, the first driving mechanism includes an active mechanism and a driven mechanism disposed above the filter chamber, and the active mechanism and the driven mechanism are respectively disposed on the front and rear sides of the filter chamber; The active mechanism includes a lead screw, an active slider disposed on the lead screw, and a servo motor drivingly coupled to the lead screw; the driven mechanism includes a guide rod, and a guide rod disposed on the guide rod Follow the slider.
进一步地,所述除渣机构包括压力调节板、支撑梁、固定座、除渣刮板以及两个立柱,所述的压力调节板、支撑梁、固定座、除渣刮板从上到下依次设置,所述固定座与除渣刮板相连,两个所述立柱的底端分别与所述固定座相连,两个所述立柱的顶端分别穿过所述支撑梁与所述压力调节板相连,在所述支撑梁与所述压力调节板之间的所述立柱上套设有弹簧,所述支撑梁与所述压力调节板之间通过调节螺栓相连;其中,所述支撑梁 的两端分别与所述主动滑块、所述从动滑块对应连接,所述除渣刮板与所述过滤网相接触。Further, the slag removing mechanism comprises a pressure regulating plate, a supporting beam, a fixing seat, a slag removing squeegee and two columns, and the pressure regulating plate, the supporting beam, the fixing seat and the slag removing squeegee are in order from top to bottom Provided that the fixing seat is connected to the slag scraping board, the bottom ends of the two columns are respectively connected to the fixing seat, and the top ends of the two columns are respectively connected to the pressure regulating plate through the supporting beam a spring is sleeved on the column between the support beam and the pressure regulating plate, and the support beam and the pressure regulating plate are connected by an adjusting bolt; wherein two ends of the supporting beam Correspondingly connected to the active slider and the driven slider respectively, the slag scraping blade is in contact with the filter mesh.
进一步地,所述往复式过滤装置还包括第一机架,所述过滤室安装在所述第一机架上,在所述第一机架上设有安装板,所述安装板设置在所述过滤室上方,所述主动机构和所述从动机构均设置在所述安装板上;所述排气式储浆装置还包括第二机架,所述储浆室设置在所述第二机架上。Further, the reciprocating filter device further includes a first frame, the filter chamber is mounted on the first frame, and a mounting plate is disposed on the first frame, and the mounting plate is disposed at the Above the filter chamber, the active mechanism and the driven mechanism are both disposed on the mounting plate; the vented slurry storage device further includes a second frame, and the slurry chamber is disposed at the second On the rack.
进一步地,所述抽真空排气机构包括与所述储浆室相连的排气管路以及与所述排气管路相连的真空泵。Further, the evacuation venting mechanism includes an exhaust line connected to the slurry chamber and a vacuum pump connected to the exhaust line.
具体地,所述过滤网将所述过滤室分隔为上部除渣过滤分室和下部浆液存储分室,所述上部除渣过滤分室为矩形槽体结构,所述下部浆液存储分室为漏斗形结构,其中所述下部浆液存储分室与所述储浆室之间通过浆液输送管路相连;在所述上部除渣过滤分室与所述下部浆液存储分室之间的结合处设有密封垫,所述过滤网设置在所述密封垫上。Specifically, the filter screen divides the filter chamber into an upper slag filter compartment and a lower slurry storage compartment, the upper slag filter compartment is a rectangular tank structure, and the lower slurry storage compartment is a funnel-shaped structure, wherein The lower slurry storage compartment is connected to the slurry chamber through a slurry delivery line; a seal is provided at a junction between the upper slag filtration compartment and the lower slurry storage compartment, the filter Disposed on the gasket.
具体地,所述上部除渣过滤分室中设有第一液位传感器,所述储浆室中设有第二液位传感器;设置在所述下部浆液存储分室出口处的所述浆液输送管路上设有第一控制阀,设置在所述储浆室进口处的所述浆液输送管路上设有第二控制阀,在所述排气管路上设有第三控制阀。Specifically, a first liquid level sensor is disposed in the upper slag filtering sub-chamber, a second liquid level sensor is disposed in the slurry storage chamber, and the slurry conveying pipeline is disposed at an outlet of the lower slurry storage sub-chamber A first control valve is disposed, and a second control valve is disposed on the slurry delivery line disposed at the inlet of the slurry chamber, and a third control valve is disposed on the exhaust line.
具体地,所述第二驱动机构包括与所述搅拌机构相连的减速电机;在所述储浆室的外部设有保温层。Specifically, the second driving mechanism includes a geared motor connected to the stirring mechanism; and an insulating layer is disposed outside the slurry chamber.
进一步地,还包括控制装置,所述控制装置包括自动控制器,所述自动控制器分别与所述的伺服电机、减速电机、真空泵、第一液位传感器、第二液位传感器、第一控制阀、第二控制阀和第三控制阀相连。Further, the device further includes a control device including an automatic controller, the automatic controller and the servo motor, the reduction motor, the vacuum pump, the first liquid level sensor, the second liquid level sensor, and the first control The valve, the second control valve and the third control valve are connected.
本发明还提供了一种蜂王浆过滤方法,采用上述的蜂王浆过滤装置,具体包括如下步骤:The invention also provides a method for filtering royal jelly, which adopts the above-mentioned royal jelly filtering device, and specifically comprises the following steps:
S1、在所述过滤室中安装所述过滤网,在所述过滤网上安装所述除渣机构,并调节所述除渣机构的压力达到预定要求,关闭所述第一控制阀;S1, installing the filter net in the filter chamber, installing the slag removing mechanism on the filter net, and adjusting the pressure of the slag removing mechanism to meet a predetermined requirement, and closing the first control valve;
S2、将解冻后的蜂王浆加入所述过滤室中,确保所述过滤室中蜂王浆液位低于预定液位上限。S2, adding the thawed royal jelly to the filtering chamber to ensure that the liquid level of the royal jelly in the filtering chamber is lower than the upper limit of the predetermined liquid level.
S3、接通电源,启动所述自动控制器,将所述除渣机构的运动速度设定为0.2~0.8m/s,将所述真空泵的真空压力设定为4~20kPa,将所述搅拌 机构的搅拌速度设定为30~50rpm;S3, turning on the power, starting the automatic controller, setting the moving speed of the slag removing mechanism to 0.2-0.8 m/s, setting the vacuum pressure of the vacuum pump to 4-20 kPa, and stirring the The stirring speed of the mechanism is set to 30 to 50 rpm;
S4、开启所述第一控制阀和所述第三控制阀,启动所述真空泵,当真空压力满足设定要求后,开启所述第二控制阀,启动所述伺服电机,所述除渣机构进行自动过滤和除渣作业,并通过所述第一液位传感器实时监控所述过滤室中的蜂王浆液位;S4, the first control valve and the third control valve are opened, the vacuum pump is activated, and when the vacuum pressure meets the set requirement, the second control valve is opened to start the servo motor, and the slag removing mechanism Performing automatic filtration and slag removal operations, and monitoring the level of the royal jelly in the filtration chamber in real time by the first liquid level sensor;
S5、当所述过滤室中的蜂王浆液位低于预定液位下限时,向所述过滤室中进行加液作业,当所述过滤室中的蜂王浆液位达到预定液位上限时,加液作业自动停止;S5. When the liquid level of the royal jelly in the filtering chamber is lower than the lower limit of the predetermined liquid level, the liquid adding operation is performed in the filtering chamber, and when the liquid level of the royal jelly in the filtering chamber reaches the upper limit of the predetermined liquid level, the liquid adding The job is automatically stopped;
S6、当所述储浆室中的液位达到预定液位后,所述第二液位传感器传输启动信号,所述自动控制器启动所述减速电机,所述搅拌机构进行蜂王浆均质、脱气作业;S6. After the liquid level in the slurry storage chamber reaches a predetermined liquid level, the second liquid level sensor transmits a start signal, and the automatic controller activates the speed reduction motor, and the stirring mechanism performs homogenization and removal of the royal jelly. Gas operation
S7、蜂王浆全部投入所述过滤室后,当所述过滤室中的蜂王浆液位低于预警液位时,所述第一液位传感器传输停止信号,所述自动控制器关闭所述第二控制阀,所述伺服电机停止工作,自动过滤和除渣作业完成;S7. After the royal jelly is all put into the filtering chamber, when the liquid level of the royal jelly in the filtering chamber is lower than the warning liquid level, the first liquid level sensor transmits a stop signal, and the automatic controller turns off the second control. Valve, the servo motor stops working, automatic filtering and slag removal operations are completed;
S8、清理所述过滤室和所述浆液输送管路内残留的蜂王浆,并收集所述过滤网内的滤渣,完成清场作业。S8. Clean the residual royal jelly in the filter chamber and the slurry conveying pipeline, and collect the filter residue in the filter net to complete the clearing operation.
本发明的上述技术方案具有如下优点:The above technical solution of the present invention has the following advantages:
本发明提供的蜂王浆过滤装置及方法,通过第一驱动机构驱动除渣机构在过滤网上进行直线往复运动,从而实现蜂王浆过滤连续生产,使得蜂王浆过滤作业实现自动化,有利于蜂王浆生产加工过程标准化。The royal jelly filtering device and method provided by the invention drive the slag removing mechanism to linearly reciprocate on the filtering net by the first driving mechanism, thereby realizing the continuous production of the royal jelly filtering, realizing the automation of the royal jelly filtering operation, and facilitating the standardization of the royal jelly production and processing process.
本发明提供的蜂王浆过滤装置及方法,通过第二驱动机构驱动搅拌机构运动,从而实现蜂王浆均质、脱气作业,并且通过抽真空排气机构来实现抽真空排气,同时提高了蜂王浆过滤效率,可实现低温快速过滤,过滤所得蜂王浆通过低温、真空、避光的储浆室进行贮存,有效减少了氧气、光照和温度对蜂王浆过滤产生的不利影响。The royal jelly filtering device and method provided by the invention drive the stirring mechanism to move by the second driving mechanism, thereby realizing the homogenization and degassing operation of the royal jelly, and the vacuuming and exhausting is realized by the vacuuming and exhausting mechanism, and the filtration efficiency of the royal jelly is improved. It can realize low-temperature rapid filtration, and the filtered royal jelly is stored in a low-temperature, vacuum, dark-proof storage chamber, which effectively reduces the adverse effects of oxygen, light and temperature on the filtration of royal jelly.
本发明提供的蜂王浆过滤装置及方法,将往复除渣与负压吸滤结合联用,在过滤室内的蜂王浆进行过滤作业时,储浆室内的蜂王浆同时完成脱气、均质作业,不仅大大缩短了蜂王浆与空气接触时间,而且有效降低了蜂王浆生产总时间,蜂王浆过滤进入储浆室后处于低氧状态,同时通过在 储浆室外部设置保温层,保持了低温储存条件,更有效保存蜂王浆功效成分。The royal jelly filtering device and method provided by the invention combines reciprocating slag and negative pressure suction filtering, and when the royal jelly in the filtering chamber is filtered, the royal jelly in the slurry chamber simultaneously completes degassing and homogenizing operation, which is not only greatly shortened The contact time between royal jelly and air is effective, and the total production time of royal jelly is effectively reduced. The royal jelly is in a low-oxygen state after being filtered into the slurry storage chamber. At the same time, by providing an insulation layer outside the slurry storage, the low-temperature storage condition is maintained, and the effect of the royal jelly is more effectively preserved. ingredient.
本发明提供的蜂王浆过滤装置及方法,采用压力可调节的除渣机构,除渣机构在往复运动中可自动刮除积累在过滤网上的滤渣,滤渣可暂存于过滤网的两侧,相比现有蜂王浆过滤方式,大大降低了滤渣二次堵塞滤网的可能,大幅提高了过滤效率和稳定性。The royal jelly filtering device and method provided by the invention adopts a pressure-adjustable slag removing mechanism, and the slag removing mechanism can automatically scrape the filter residue accumulated on the filter net during the reciprocating motion, and the filter residue can be temporarily stored on both sides of the filter net. The existing royal jelly filtration mode greatly reduces the possibility of secondary clogging of the filter slag, and greatly improves the filtration efficiency and stability.
本发明提供的蜂王浆过滤装置及方法,采用自动控制器控制第一驱动机构、第二驱动机构、抽真空排气机构以及各个控制阀门的工作,同时采用液位传感器来分别监控过滤室和储浆室内的蜂王浆液位,不仅控制精度高,可靠性强,而且实现了蜂王浆自动高效连续过滤,降低了生产成本。The royal jelly filtering device and method provided by the invention adopts an automatic controller to control the working of the first driving mechanism, the second driving mechanism, the vacuuming exhausting mechanism and the respective control valves, and simultaneously adopts the liquid level sensor to separately monitor the filtering chamber and the slurry. The indoor royal jelly liquid level not only has high control precision and high reliability, but also realizes automatic high-efficiency continuous filtration of royal jelly, which reduces production cost.
图1是本发明实施例蜂王浆过滤装置的结构示意图;1 is a schematic structural view of a royal jelly filtering device according to an embodiment of the present invention;
图2是本发明实施例蜂王浆过滤装置图1中局部A的放大图;Figure 2 is an enlarged view of a portion A of Figure 1 of the royal jelly filtration device of the embodiment of the present invention;
图3是本发明实施例蜂王浆过滤装置中往复式过滤装置的俯视图;3 is a top plan view of a reciprocating filter device in a royal jelly filter device according to an embodiment of the present invention;
图4是本发明实施例蜂王浆过滤装置中搅拌机构的示意图。4 is a schematic view of a stirring mechanism in a royal jelly filtration device according to an embodiment of the present invention.
图中:1:过滤室;101:上部除渣过滤分室;102:下部浆液存储分室;2:过滤网;3:除渣机构;301:压力调节板;302:支撑梁;303:固定座;304:除渣刮板;305:立柱;306:弹簧;307:调节螺栓;4:储浆室;5:搅拌机构;6:减速电机;7:丝杠;8:主动滑块;9:伺服电机;10:导杆;11:从动滑块;12:第一机架;13:安装板;14:第二机架;15:排气管路;16:真空泵;17:浆液输送管路;18:密封垫;19:第一液位传感器;20:第二液位传感器;21:第一控制阀;22:第二控制阀;23:第三控制阀;24:自动控制器;25:保温层。In the figure: 1: filter chamber; 101: upper slag filter compartment; 102: lower slurry storage compartment; 2: filter; 3: slag removal mechanism; 301: pressure regulation plate; 302: support beam; 303: fixed seat; 304: slag scraping plate; 305: column; 306: spring; 307: adjusting bolt; 4: pulping chamber; 5: stirring mechanism; 6: geared motor; 7: screw; 8: active slider; Motor; 10: guide rod; 11: driven slider; 12: first frame; 13: mounting plate; 14: second frame; 15: exhaust pipe; 16: vacuum pump; 17: slurry conveying pipe 18: seal; 19: first level sensor; 20: second level sensor; 21: first control valve; 22: second control valve; 23: third control valve; 24: automatic controller; :Insulation.
为使本发明实施例的目的、技术方案和优点更加清楚,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,所描述的实施例是本发明的一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动的前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described in conjunction with the drawings in the embodiments of the present invention. It is a part of the embodiment of the invention, not all of the embodiments. All other embodiments obtained by a person of ordinary skill in the art based on the embodiments of the present invention without creative efforts are within the scope of the present invention.
如图1-4所示,本发明实施例提供一种蜂王浆过滤装置,包括往复式过滤装置以及与所述往复式过滤装置相连的排气式储浆装置。As shown in FIG. 1-4, an embodiment of the present invention provides a royal jelly filtering device including a reciprocating filtering device and a venting slurry storage device connected to the reciprocating filtering device.
所述往复式过滤装置包括过滤室1、设置在所述过滤室1中的过滤网2、设置在所述过滤网2上的除渣机构3、以及驱动所述除渣机构3在所述过滤网2上进行直线往复运动的第一驱动机构。The reciprocating filter device includes a filter chamber 1, a filter screen 2 disposed in the filter chamber 1, a slag removal mechanism 3 disposed on the filter screen 2, and a drive for the slag removal mechanism 3 at the filter A first drive mechanism for linear reciprocating motion on the net 2.
所述排气式储浆装置包括储浆室4、设置在所述储浆室4中的搅拌机构5、驱动所述搅拌机构5进行搅拌动作的第二驱动机构、以及与所述储浆室4相连的抽真空排气机构。The venting type slurry storage device includes a slurry storage chamber 4, a stirring mechanism 5 disposed in the slurry storage chamber 4, a second driving mechanism that drives the stirring mechanism 5 to perform a stirring operation, and a storage chamber 4 connected vacuum exhaust mechanism.
本发明实施例所述的蜂王浆过滤装置,通过所述第一驱动机构驱动所述除渣机构3在所述过滤网2上进行直线往复运动,从而实现蜂王浆连续过滤生产,使得蜂王浆过滤作业实现自动化和标准作业,有利于蜂王浆生产过程标准化。通过所述第二驱动机构驱动所述搅拌机构5进行搅拌运动,通过所述抽真空排气机构来实现抽真空排气,从而实现蜂王浆均质、脱气作业,同时提高了蜂王浆过滤效率。The royal jelly filtering device according to the embodiment of the present invention drives the slag removal mechanism 3 to perform linear reciprocating motion on the filter net 2 by the first driving mechanism, thereby realizing continuous filtration production of royal jelly, thereby realizing automatic filtration operation of royal jelly. And standard work, which is conducive to the standardization of the royal jelly production process. The stirring mechanism is driven by the second driving mechanism to perform a stirring motion, and the vacuuming and exhausting mechanism is used to realize vacuuming and exhausting, thereby realizing homogenization and degassing operation of the royal jelly, and improving the filtration efficiency of the royal jelly.
本发明实施例所述的蜂王浆过滤装置,将往复除渣与负压吸滤结合联用,在所述过滤室1内的蜂王浆进行过滤作业时,所述储浆室4内的蜂王浆同时完成脱气、均质作业,不仅大大缩短了蜂王浆与空气接触时间,而且有效降低了蜂王浆生产总时间,蜂王浆过滤进入所述储浆室4后处于真空、低氧、避光状态,从而有效保护了蜂王浆功效成分。The royal jelly filtering device according to the embodiment of the present invention combines the reciprocating slag and the negative pressure suction filter. When the royal jelly in the filtering chamber 1 is subjected to the filtering operation, the royal jelly in the slurry storage chamber 4 is simultaneously removed. Gas and homogenization work not only greatly shortens the contact time between royal jelly and air, but also effectively reduces the total production time of royal jelly. After the royal jelly is filtered into the slurry storage chamber 4, it is in a vacuum, low oxygen and dark state, thus effectively protecting the royal jelly. Functional ingredients.
进一步来说,所述第一驱动机构包括设置在所述过滤室1上方的主动机构和从动机构,所述主动机构和所述从动机构分别对应设置在所述过滤室1的前后两侧。Further, the first driving mechanism includes an active mechanism and a driven mechanism disposed above the filter chamber 1, and the active mechanism and the driven mechanism are respectively disposed on the front and rear sides of the filter chamber 1 respectively. .
其中,所述主动机构包括丝杆7、设置在所述丝杠7上的主动滑块8、以及与所述丝杠7驱动连接的伺服电机9,所述伺服电机9驱动所述丝杠7进行顺时针或逆时针转动,进而带动所述主动滑块8沿所述丝杠7进行直线往复运动。The active mechanism includes a lead screw 7, an active slider 8 disposed on the lead screw 7, and a servo motor 9 drivingly coupled to the lead screw 7, the servo motor 9 driving the lead screw 7 The clockwise or counterclockwise rotation is performed to drive the active slider 8 to linearly reciprocate along the lead screw 7.
其中,所述从动机构包括导杆10、以及设置在所述导杆10上的从动滑块11,所述从动滑块11能够沿所述导杆10进行直线往复运动。The driven mechanism includes a guide rod 10 and a driven slider 11 disposed on the guide rod 10, and the driven slider 11 can linearly reciprocate along the guide rod 10.
进一步来说,所述除渣机构3包括压力调节板301、支撑梁302、固定座303、除渣刮板304以及两个立柱305,所述的压力调节板301、支撑 梁302、固定座303、除渣刮板304从上到下依次设置,所述固定座303与除渣刮板304相连,两个所述立柱305的底端分别与所述固定座303相连,两个所述立柱305的顶端分别穿过所述支撑梁302与所述压力调节板301相连,在所述支撑梁302与所述压力调节板301之间的所述立柱305上套设有弹簧306,所述支撑梁302与所述压力调节板301之间通过调节螺栓307相连。Further, the slag removing mechanism 3 includes a pressure regulating plate 301, a support beam 302, a fixing base 303, a slag removing blade 304, and two columns 305, the pressure regulating plate 301, the support beam 302, and the fixing base 303. The slag scrapers 304 are disposed in order from top to bottom, and the fixing base 303 is connected to the slag scraping plate 304. The bottom ends of the two struts 305 are respectively connected to the fixing base 303, and the two columns 305 are respectively connected. The top end is connected to the pressure regulating plate 301 through the support beam 302, and the spring 306 is sleeved on the column 305 between the support beam 302 and the pressure regulating plate 301. 302 is connected to the pressure regulating plate 301 by an adjusting bolt 307.
其中,所述支撑梁302的两端分别与所述主动滑块8、所述从动滑块11对应连接,从而通过所述主动滑块8和所述从动滑块11带动所述除渣机构3进行直线往复运动。The two ends of the support beam 302 are respectively connected to the active slider 8 and the driven slider 11 to drive the slag through the active slider 8 and the driven slider 11 . The mechanism 3 performs a linear reciprocating motion.
其中,所述除渣刮板304与所述过滤网2相接触,通过所述除渣机构3进行直线往复运动,来实现对蜂王浆的连续过滤作业。通过所述调节螺栓307来调整所述支撑梁302与所述压力调节板301之间的距离,从而改变所述除渣刮板304施加在所述过滤网2上的轴向压力。Wherein, the slag scraping blade 304 is in contact with the filter net 2, and linear reciprocating motion is performed by the dross removing mechanism 3 to realize continuous filtering operation on the royal jelly. The distance between the support beam 302 and the pressure regulating plate 301 is adjusted by the adjusting bolt 307, thereby changing the axial pressure exerted by the dross removing blade 304 on the filter screen 2.
本发明实施例所述的蜂王浆过滤装置,所述除渣机构3的压力可自行调节,所述除渣机构3在往复运动中可自动刮除积累在所述过滤网2上的滤渣,滤渣可暂存于所述过滤网2的两侧,从而大大降低了滤渣二次堵塞滤网的可能,进而大幅提高了过滤效率和稳定性。In the royal jelly filtering device of the embodiment of the invention, the pressure of the slag removing mechanism 3 can be adjusted by itself, and the slag removing mechanism 3 can automatically scrape the filter residue accumulated on the filter net 2 during the reciprocating motion, and the filter residue can be Temporarily stored on both sides of the filter net 2, thereby greatly reducing the possibility of the filter residue secondary clogging the filter screen, thereby greatly improving the filtration efficiency and stability.
进一步来说,所述往复式过滤装置还包括第一机架12,所述过滤室1安装在所述第一机架12上,在所述第一机架12上设有安装板13,所述安装板13设置在所述过滤室1上方,所述主动机构和所述从动机构均设置在所述安装板13上。所述排气式储浆装置还包括第二机架14,所述储浆室4设置在所述第二机架14上。Further, the reciprocating filter device further includes a first frame 12, the filter chamber 1 is mounted on the first frame 12, and a mounting plate 13 is disposed on the first frame 12. The mounting plate 13 is disposed above the filter chamber 1, and the active mechanism and the driven mechanism are both disposed on the mounting plate 13. The vented slurry storage device further includes a second frame 14 on which the slurry chamber 4 is disposed.
更进一步来说,所述抽真空排气机构包括与所述储浆室4相连的排气管路15以及与所述排气管路15相连的真空泵16。Further, the evacuation venting mechanism includes an exhaust line 15 connected to the slurry chamber 4 and a vacuum pump 16 connected to the exhaust line 15.
具体来说,所述过滤网2将所述过滤室1分隔为上部除渣过滤分室101和下部浆液存储分室102,所述上部除渣过滤分室101为矩形槽体结构,所述下部浆液存储分室102为漏斗形结构,其中所述下部浆液存储分室102与所述储浆室4之间通过浆液输送管路17相连。Specifically, the filter screen 2 divides the filter chamber 1 into an upper slag filter compartment 101 and an lower slurry storage compartment 102, and the upper slag filter compartment 101 is a rectangular tank structure, and the lower slurry storage compartment 102 is a funnel-shaped structure in which the lower slurry storage compartment 102 and the slurry storage chamber 4 are connected by a slurry delivery line 17.
其中,在所述上部除渣过滤分室101与所述下部浆液存储分室102之间的结合处设有密封垫18,所述过滤网2设置在所述密封垫18上,所述 密封垫18采用硅胶材料制成,厚度优选设置为5~8mm。通过设置所述密封垫18,能够确保所述上部除渣过滤分室101中的蜂王浆不会从所述过滤网2的四周边缘缝隙流入到所述下部浆液存储分室102中,保障了过滤效果。Wherein, a seal 18 is disposed at a junction between the upper slag filtering compartment 101 and the lower slurry storage compartment 102, and the filter 2 is disposed on the gasket 18, and the gasket 18 is Made of a silicone material, the thickness is preferably set to 5 to 8 mm. By providing the gasket 18, it is possible to ensure that the royal jelly in the upper dross removing filter compartment 101 does not flow from the peripheral edge gap of the filter net 2 into the lower slurry storage compartment 102, thereby ensuring the filtering effect.
具体来说,所述上部除渣过滤分室101中设有第一液位传感器19,所述储浆室4中设有第二液位传感器20。设置在所述下部浆液存储分室102出口处的所述浆液输送管路17上设有第一控制阀21,设置在所述储浆室4进口处的所述浆液输送管路17上设有第二控制阀22,在所述排气管路15上设有第三控制阀23。Specifically, a first liquid level sensor 19 is disposed in the upper slag filtering compartment 101, and a second liquid level sensor 20 is disposed in the slurry chamber 4. a first control valve 21 is disposed on the slurry delivery line 17 disposed at the outlet of the lower slurry storage compartment 102, and the slurry delivery line 17 disposed at the inlet of the slurry storage chamber 4 is provided with a first The second control valve 22 is provided with a third control valve 23 on the exhaust line 15.
具体来说,所述第二驱动机构包括与所述搅拌机构5相连的减速电机6。Specifically, the second drive mechanism includes a reduction motor 6 connected to the agitation mechanism 5.
更进一步来说,本发明实施例所述的蜂王浆过滤装置,还包括控制装置,所述控制装置包括自动控制器24,所述自动控制器24分别与所述的伺服电机9、减速电机6、真空泵16、第一液位传感器19、第二液位传感器20、第一控制阀21、第二控制阀22和第三控制阀23相连。Further, the royal jelly filtering device according to the embodiment of the present invention further includes a control device, the control device includes an automatic controller 24, and the automatic controller 24 and the servo motor 9 and the reduction motor 6, respectively. The vacuum pump 16, the first level sensor 19, the second level sensor 20, the first control valve 21, the second control valve 22, and the third control valve 23 are connected.
本发明实施例所述的蜂王浆过滤装置,采用所述自动控制器24来控制所述的第一驱动机构、第二驱动机构、抽真空排气机构以及各个控制阀门的工作,同时利用所述的第一液位传感器19和第二液位传感器20来分别监控所述过滤室1和所述储浆室4内的蜂王浆液位,不仅控制精度高,可靠性强,而且实现了蜂王浆自动高效连续过滤,降低了生产成本。The royal jelly filtering device according to the embodiment of the present invention uses the automatic controller 24 to control the operations of the first driving mechanism, the second driving mechanism, the vacuum exhausting mechanism, and the respective control valves, while utilizing the The first liquid level sensor 19 and the second liquid level sensor 20 respectively monitor the liquid level of the royal jelly in the filter chamber 1 and the slurry storage chamber 4, which not only has high control precision and high reliability, but also realizes automatic and efficient continuous continuous operation of royal jelly. Filtration reduces production costs.
此外,所述储浆室4优选采用316L不锈钢板材制成,壁厚设置为6~10mm。Further, the slurry chamber 4 is preferably made of 316L stainless steel sheet and has a wall thickness of 6 to 10 mm.
此外,所述过滤室1采用食品级亚克力不透光材料热塑成型,所述过滤室1壁厚设置为8~12mm,而所述下部浆液存储分室102的倾斜角度设置为20~30度。Further, the filter chamber 1 is thermoformed using a food grade acrylic opaque material, the filter chamber 1 has a wall thickness of 8 to 12 mm, and the lower slurry storage compartment 102 has an angle of inclination of 20 to 30 degrees.
此外,所述过滤网2网目数为80~120目。所述过滤网2的四周采用食品级亚克力材料固定,厚度设置为8~12mm。Further, the number of meshes of the filter network 2 is 80 to 120 mesh. The periphery of the filter net 2 is fixed by a food grade acrylic material, and the thickness is set to 8 to 12 mm.
此外,所述除渣刮板304采用食品级硅胶材料制成,厚度设置为15~25mm。所述固定座303采用食品级亚克力材料制成,厚度设置为20~30mm。所述立柱305采用316L不锈钢板材制成,直径设置为 20~25mm。In addition, the slag scraping blade 304 is made of a food grade silica gel material and has a thickness of 15 to 25 mm. The fixing seat 303 is made of food grade acrylic material and has a thickness of 20-30 mm. The column 305 is made of 316L stainless steel plate and has a diameter of 20 to 25 mm.
本发明实施例所述的蜂王浆过滤装置,所述过滤室1和所述储浆室4均采用自流设计,无清理死角,减少了蜂王浆损耗。而与蜂王浆接触部件选用食品级亚克力材料和316L不锈钢材料制成,有效降低了蜂王浆过滤及储存过程中的化学反应所产生的不利影响。In the royal jelly filtering device according to the embodiment of the present invention, the filtering chamber 1 and the slurry storage chamber 4 are all designed in a self-flowing manner, and no dead angle is cleaned, thereby reducing the loss of royal jelly. The contact parts with royal jelly are made of food grade acrylic material and 316L stainless steel material, which effectively reduces the adverse effects of chemical reaction during the filtration and storage of royal jelly.
此外,在所述储浆室4的外部设有保温层25,所述保温层25的厚度为60~80mm。通过设置所述保温层25,保证了所述储浆室4内的低温储存条件,从而更加有效地保存蜂王浆功效成分。Further, an insulating layer 25 is provided outside the slurry chamber 4, and the insulating layer 25 has a thickness of 60 to 80 mm. By providing the insulating layer 25, the low temperature storage conditions in the slurry chamber 4 are ensured, thereby more effectively preserving the royal jelly efficacy component.
本发明实施例提供一种蜂王浆过滤方法,该方法采用上述实施例的蜂王浆过滤装置进行蜂王浆过滤操作,具体包括如下步骤:The embodiment of the present invention provides a method for filtering a royal jelly. The method uses the royal jelly filter device of the above embodiment to perform a royal jelly filtering operation, and specifically includes the following steps:
S1、在所述过滤室1中安装所述过滤网2,在所述过滤网2上安装所述除渣机构3,调节所述除渣机构3的压力达到预定要求,关闭所述第一控制阀21。S1, the filter net 2 is installed in the filter chamber 1, and the dross removing mechanism 3 is installed on the filter net 2, and the pressure of the dross removing mechanism 3 is adjusted to meet a predetermined requirement, and the first control is turned off. Valve 21.
S2、将解冻后的蜂王浆加入所述过滤室1中,确保所述过滤室1中蜂王浆液位低于预定液位上限。S2, adding the thawed royal jelly to the filter chamber 1 to ensure that the liquid level of the royal jelly in the filter chamber 1 is lower than the upper limit of the predetermined liquid level.
S3、接通电源,启动所述自动控制器24,将所述除渣机构3的运动速度设定为0.2~0.8m/s,将所述真空泵16的真空压力设定为4~20kPa,将所述搅拌机构5的搅拌速度设定为30~50rpm。S3, turning on the power, starting the automatic controller 24, setting the moving speed of the dross removing mechanism 3 to 0.2 to 0.8 m/s, and setting the vacuum pressure of the vacuum pump 16 to 4 to 20 kPa, The stirring speed of the stirring mechanism 5 is set to 30 to 50 rpm.
S4、开启所述第一控制阀21和所述第三控制阀23,启动所述真空泵16,当真空压力满足设定要求后,开启所述第二控制阀22,启动所述伺服电机9,所述除渣机构3进行自动过滤和除渣作业,并通过所述第一液位传感器19实时监控所述过滤室1中的蜂王浆液位。S4, the first control valve 21 and the third control valve 23 are opened, the vacuum pump 16 is activated, and when the vacuum pressure meets the set requirement, the second control valve 22 is opened, and the servo motor 9 is activated. The slag removing mechanism 3 performs an automatic filtering and slag removing operation, and monitors the level of the royal jelly in the filtering chamber 1 in real time by the first liquid level sensor 19.
S5、当所述过滤室1中的蜂王浆液位低于预定液位下限时,向所述过滤室1中进行加液作业,可采用自动加液或者手动加液方式进行加液操作。当所述过滤室1中的蜂王浆液位达到预定液位上限时,加液作业自动停止。S5. When the liquid level of the royal jelly in the filtering chamber 1 is lower than the lower limit of the predetermined liquid level, the liquid adding operation is performed in the filtering chamber 1, and the liquid adding operation may be performed by automatic liquid adding or manual liquid adding. When the liquid level of the royal jelly in the filter chamber 1 reaches the upper limit of the predetermined liquid level, the liquid filling operation is automatically stopped.
S6、当所述储浆室4中的液位达到预定液位后,所述第二液位传感器20传输启动信号,所述自动控制器24启动所述减速电机6,所述搅拌机构5进行蜂王浆均质、脱气作业。S6. After the liquid level in the slurry storage chamber 4 reaches a predetermined liquid level, the second liquid level sensor 20 transmits a start signal, and the automatic controller 24 activates the speed reduction motor 6, and the stirring mechanism 5 performs The royal jelly is homogenized and degassed.
S7、在蜂王浆全部投入所述过滤室1之后,当所述过滤室1中的蜂王浆液位低于预警液位时,所述第一液位传感器19传输停止信号,所述自 动控制器24关闭所述第二控制阀22,所述伺服电机9停止工作,自动过滤和除渣作业完成。S7. After the royal jelly is all put into the filter chamber 1, when the liquid level of the royal jelly in the filter chamber 1 is lower than the warning liquid level, the first liquid level sensor 19 transmits a stop signal, and the automatic controller 24 is turned off. The second control valve 22, the servo motor 9 stops working, and the automatic filtering and slag removal operations are completed.
S8、清理所述过滤室1和所述浆液输送管路17内残留的蜂王浆,并收集所述过滤网2上的滤渣,完成清场作业。S8, cleaning the royal jelly remaining in the filter chamber 1 and the slurry conveying pipeline 17, and collecting the filter residue on the filter net 2 to complete the clearing operation.
下面通过两个实际应用过程中的实施例来对本发明所述的蜂王浆过滤装置及方法进行具体说明。The royal jelly filtering device and method according to the present invention will be specifically described below by way of embodiments in two practical applications.
第一实施例First embodiment
将300公斤油菜花期蜂王浆充分解冻,完全解冻后备用。The 300 kg of rapeseed royal jelly is fully thawed and completely thawed for later use.
在所述过滤室1中安装所述过滤网2,其中所述过滤网2的目数为100目,调节所述除渣机构3的压力达到预定要求,关闭所述第一控制阀21。The filter screen 2 is installed in the filter chamber 1, wherein the filter net 2 has a mesh number of 100 mesh, and the pressure of the dross removing mechanism 3 is adjusted to meet a predetermined requirement, and the first control valve 21 is closed.
将充分解冻的油菜蜂王浆泵入所述过滤室1内,使蜂王浆液位稍低于预定液位上限。The fully thawed canola royal jelly is pumped into the filter chamber 1 such that the royal jelly level is slightly below the upper limit of the predetermined level.
接通电源,启动所述自动控制器24,将所述除渣机构3的运动速度设定为0.3m/s,将所述真空泵16的真空压力设定为10kPa~15kPa,将所述搅拌机构5的搅拌速度设定为35rpm。Turning on the power, starting the automatic controller 24, setting the moving speed of the dross removing mechanism 3 to 0.3 m/s, setting the vacuum pressure of the vacuum pump 16 to 10 kPa to 15 kPa, and the stirring mechanism The stirring speed of 5 was set to 35 rpm.
开启所述第一控制阀21和所述第三控制阀23,启动所述真空泵16,当真空压力低于15kPa后,开启所述第二控制阀22,同时启动所述伺服电机9,所述除渣机构3进行自动过滤和除渣作业,通过所述第一液位传感器19实时传输所述过滤室1中的蜂王浆液位,所述自动控制器24的实时显示所述过滤室1中的蜂王浆液位数值。Opening the first control valve 21 and the third control valve 23, starting the vacuum pump 16, and when the vacuum pressure is lower than 15 kPa, opening the second control valve 22, and simultaneously starting the servo motor 9, The slag removing mechanism 3 performs an automatic filtering and slag removing operation, and the royal liquid level in the filtering chamber 1 is transmitted in real time through the first liquid level sensor 19, and the automatic controller 24 displays the real time in the filtering chamber 1 Royal jelly level value.
过滤作业5分钟后,所述过滤室1中的蜂王浆液位低于预定液位下限,自动控制系统执行自动加料作业,向所述过滤室1中进行自动加液作业,当所述过滤室1中的蜂王浆液位达到预定液位上限时,加液作业自动停止。After 5 minutes of the filtering operation, the liquid level of the royal jelly in the filtering chamber 1 is lower than the lower limit of the predetermined liquid level, and the automatic control system performs an automatic feeding operation to perform an automatic liquid adding operation to the filtering chamber 1 when the filtering chamber 1 When the liquid level of the royal jelly reaches the upper limit of the predetermined liquid level, the liquid filling operation is automatically stopped.
所述往复式过滤装置工作18分钟后,所述储浆室4中的液位达到预定液位,所述第二液位传感器20传输启动信号,所述自动控制器24启动所述减速电机6,所述搅拌机构5进行蜂王浆均质、脱气作业。After the reciprocating filter device is operated for 18 minutes, the liquid level in the slurry storage chamber 4 reaches a predetermined liquid level, the second liquid level sensor 20 transmits an activation signal, and the automatic controller 24 activates the reduction motor 6 The stirring mechanism 5 performs homogenization and degassing operation of the royal jelly.
所述往复式过滤装置工作35分钟后,蜂王浆原料已全部投入所述过滤室1,当所述过滤室1中的蜂王浆液位低于预警液位时,所述第一液位传感器19传输停止信号,所述自动控制器24关闭所述第二控制阀22,所述伺服电机9停止工作,自动过滤和除渣作业完成,过滤总时间为41分 钟。After the reciprocating filter device is operated for 35 minutes, the raw material of the royal jelly has all been put into the filter chamber 1. When the liquid level of the royal jelly in the filter chamber 1 is lower than the warning liquid level, the first liquid level sensor 19 stops transmitting. Signal, the automatic controller 24 closes the second control valve 22, the servo motor 9 stops working, the automatic filtration and slag removal operations are completed, and the total filtration time is 41 minutes.
清理所述过滤室1和所述浆液输送管路17内残留的蜂王浆,并收集所述过滤网2上的滤渣,完成清场作业。The royal jelly remaining in the filter chamber 1 and the slurry transfer line 17 is cleaned, and the filter residue on the filter net 2 is collected to complete the clearing operation.
过滤结果:过滤后的油菜蜂王浆未见蜂尸体、蜂蜡渣和灰尘等黑点杂质,无气泡,品质均一,有光泽。Filtration results: The filtered royal jelly royal jelly has no black spots such as bee carcasses, beeswax residue and dust, no bubbles, uniform quality and luster.
第二实施例Second embodiment
将240公斤荆条花期蜂王浆充分解冻,完全解冻后备用。The 240 kg of Viburnum Royal Jelly is fully thawed and completely thawed for later use.
在所述过滤室1中安装所述过滤网2,其中所述过滤网2的目数为120目,调节所述除渣机构3的压力达到预定要求,关闭所述第一控制阀21。The filter screen 2 is installed in the filter chamber 1, wherein the filter net 2 has a mesh number of 120 mesh, and the pressure of the dross removing mechanism 3 is adjusted to meet a predetermined requirement, and the first control valve 21 is closed.
将充分解冻的荆条蜂王浆泵入所述过滤室1内,使蜂王浆液位稍低于预定液位上限。The fully thawed Royal Jelly Royal Jelly is pumped into the filter chamber 1 such that the royal jelly level is slightly below the upper limit of the predetermined level.
接通电源,启动所述自动控制器24,将所述除渣机构3的运动速度设定为0.2m/s,将所述真空泵16的真空压力设定为12kPa~18kPa,将所述搅拌机构5的搅拌速度设定为48rpm。Turning on the power, starting the automatic controller 24, setting the moving speed of the dross removing mechanism 3 to 0.2 m/s, and setting the vacuum pressure of the vacuum pump 16 to 12 kPa to 18 kPa, and the stirring mechanism The stirring speed of 5 was set to 48 rpm.
开启所述第一控制阀21和所述第三控制阀23,启动所述真空泵16,当真空压力低于18kPa后,开启所述第二控制阀22,同时启动所述伺服电机9,所述除渣机构3进行自动过滤和除渣作业,通过所述第一液位传感器19实时传输所述过滤室1中的蜂王浆液位,所述自动控制器24的实时显示所述过滤室1中的蜂王浆液位数值。Opening the first control valve 21 and the third control valve 23, starting the vacuum pump 16, and when the vacuum pressure is lower than 18 kPa, opening the second control valve 22, and simultaneously starting the servo motor 9, The slag removing mechanism 3 performs an automatic filtering and slag removing operation, and the royal liquid level in the filtering chamber 1 is transmitted in real time through the first liquid level sensor 19, and the automatic controller 24 displays the real time in the filtering chamber 1 Royal jelly level value.
过滤作业6分钟后,所述过滤室1中的蜂王浆液位低于预定液位下限,自动控制系统执行自动加料作业,向所述过滤室1中进行自动加液作业,当所述过滤室1中的蜂王浆液位达到预定液位上限时,加液作业自动停止。After 6 minutes of the filtering operation, the liquid level of the royal jelly in the filtering chamber 1 is lower than the lower limit of the predetermined liquid level, and the automatic control system performs an automatic feeding operation, and an automatic liquid adding operation is performed in the filtering chamber 1, when the filtering chamber 1 When the liquid level of the royal jelly reaches the upper limit of the predetermined liquid level, the liquid filling operation is automatically stopped.
所述往复式过滤装置工作20分钟后,所述储浆室4中的液位达到预定液位,所述第二液位传感器20传输启动信号,所述自动控制器24启动所述减速电机6,所述搅拌机构5进行蜂王浆均质、脱气作业。After the reciprocating filter device is operated for 20 minutes, the liquid level in the slurry storage chamber 4 reaches a predetermined liquid level, the second liquid level sensor 20 transmits an activation signal, and the automatic controller 24 activates the reduction motor 6 The stirring mechanism 5 performs homogenization and degassing operation of the royal jelly.
所述往复式过滤装置工作34分钟后,蜂王浆原料已全部投入所述过滤室1,当所述过滤室1中的蜂王浆液位低于预警液位时,所述第一液位传感器19传输停止信号,所述自动控制器24关闭所述第二控制阀22,所述伺服电机9停止工作,自动过滤和除渣作业完成,过滤总时间38分钟。After the reciprocating filter device is operated for 34 minutes, the raw material of the royal jelly has all been put into the filter chamber 1. When the liquid level of the royal jelly in the filter chamber 1 is lower than the warning liquid level, the first liquid level sensor 19 stops transmitting. Signal, the automatic controller 24 closes the second control valve 22, the servo motor 9 stops working, the automatic filtration and slag removal operations are completed, and the total filtration time is 38 minutes.
清理所述过滤室1和所述浆液输送管路17内残留的蜂王浆,并收集 所述过滤网2上的滤渣,完成清场作业。The royal jelly remaining in the filtration chamber 1 and the slurry delivery line 17 is cleaned, and the filter residue on the filter 2 is collected to complete the clearing operation.
过滤结果:过滤后的荆条蜂王浆未见蜂尸体、蜂蜡渣和灰尘等黑点杂质,无气泡,品质均一,有光泽。Filtration results: The filtered royal jelly royal jelly has no black spots such as bee carcasses, beeswax residue and dust, no bubbles, uniform quality and luster.
综上所述,本发明实施例所述的蜂王浆过滤装置及方法,能够实现蜂王浆过滤连续生产,通过往复除渣与负压吸滤相结合的方式来提高蜂王浆过滤效率,过滤所得蜂王浆贮存于低温、真空、避光的环境中,有效减少了氧气、光照和温度对蜂王浆过滤产生的不利影响,同时实现了蜂王浆过滤作业的自动化,有利于蜂王浆生产加工过程标准化。In summary, the royal jelly filtering device and method according to the embodiments of the present invention can realize the continuous production of royal jelly filtration, and combine the reciprocating slag and the negative pressure suction filtration to improve the filtration efficiency of the royal jelly, and the filtered royal jelly is stored at a low temperature. In the vacuum and light-proof environment, the adverse effects of oxygen, light and temperature on the filtration of royal jelly are effectively reduced, and the automation of the royal jelly filtration operation is realized, which is conducive to the standardization of the production process of royal jelly.
最后应说明的是:以上实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的精神和范围。It should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention, and are not limited thereto; although the present invention has been described in detail with reference to the foregoing embodiments, those skilled in the art should understand that The technical solutions described in the foregoing embodiments are modified, or the equivalents of the technical features are replaced. The modifications and substitutions do not depart from the spirit and scope of the technical solutions of the embodiments of the present invention.
Claims (10)
- 一种蜂王浆过滤装置,其特征在于:包括往复式过滤装置以及与所述往复式过滤装置相连的排气式储浆装置;A royal jelly filtering device, comprising: a reciprocating filtering device; and a venting slurry storage device connected to the reciprocating filtering device;其中,所述往复式过滤装置包括过滤室、设置在所述过滤室中的过滤网、设置在所述过滤网上的除渣机构、以及驱动所述除渣机构在所述过滤网上进行直线往复运动的第一驱动机构;Wherein the reciprocating filter device comprises a filter chamber, a filter mesh disposed in the filter chamber, a slag removing mechanism disposed on the filter mesh, and driving the slag removing mechanism to perform linear reciprocating motion on the filter mesh First drive mechanism;所述排气式储浆装置包括储浆室、设置在所述储浆室中的搅拌机构、驱动所述搅拌机构进行搅拌动作的第二驱动机构、以及与所述储浆室相连的抽真空排气机构。The vented slurry storage device includes a slurry storage chamber, a stirring mechanism disposed in the slurry storage chamber, a second driving mechanism that drives the stirring mechanism to perform a stirring operation, and an evacuation vacuum connected to the slurry storage chamber Exhaust mechanism.
- 根据权利要求1所述的蜂王浆过滤装置,其特征在于:所述第一驱动机构包括设置在所述过滤室上方的主动机构和从动机构,所述主动机构和所述从动机构分别对应设置在所述过滤室的前后两侧;其中,所述主动机构包括丝杆、设置在所述丝杠上的主动滑块、以及与所述丝杠驱动连接的伺服电机;所述从动机构包括导杆、以及设置在所述导杆上的从动滑块。The royal jelly filtering device according to claim 1, wherein the first driving mechanism comprises an active mechanism and a driven mechanism disposed above the filtering chamber, and the active mechanism and the driven mechanism are respectively correspondingly arranged. On the front and rear sides of the filter chamber; wherein the active mechanism includes a lead screw, an active slider disposed on the lead screw, and a servo motor drivingly coupled to the lead screw; the driven mechanism includes a guide rod, and a driven slider disposed on the guide rod.
- 根据权利要求2所述的蜂王浆过滤装置,其特征在于:所述除渣机构包括压力调节板、支撑梁、固定座、除渣刮板以及两个立柱,所述的压力调节板、支撑梁、固定座、除渣刮板从上到下依次设置,所述固定座与除渣刮板相连,两个所述立柱的底端分别与所述固定座相连,两个所述立柱的顶端分别穿过所述支撑梁与所述压力调节板相连,在所述支撑梁与所述压力调节板之间的所述立柱上套设有弹簧,所述支撑梁与所述压力调节板之间通过调节螺栓相连;其中,所述支撑梁的两端分别与所述主动滑块、所述从动滑块对应连接,所述除渣刮板与所述过滤网相接触。The royal jelly filtering device according to claim 2, wherein the slag removing mechanism comprises a pressure regulating plate, a supporting beam, a fixing seat, a slag removing squeegee and two columns, the pressure regulating plate, the supporting beam, The fixing seat and the slag removing squeegee are disposed in order from top to bottom, and the fixing seat is connected with the slag removing squeegee, and the bottom ends of the two of the vertical columns are respectively connected with the fixing seat, and the top ends of the two columns are respectively worn The support beam is connected to the pressure regulating plate, and a spring is sleeved on the column between the support beam and the pressure regulating plate, and the support beam and the pressure regulating plate are adjusted The two ends of the support beam are respectively connected to the active sliding block and the driven sliding block, and the slag removing squeegee is in contact with the filtering net.
- 根据权利要求3所述的蜂王浆过滤装置,其特征在于:所述往复式过滤装置还包括第一机架,所述过滤室安装在所述第一机架上,在所述第一机架上设有安装板,所述安装板设置在所述过滤室上方,所述主动机构和所述从动机构均设置在所述安装板上;所述排气式储浆装置还包括第二机架,所述储浆室设置在所述第二机架上。The apparatus for filtering royal jelly according to claim 3, wherein said reciprocating filter device further comprises a first frame, said filter chamber being mounted on said first frame, said first frame a mounting plate is disposed, the mounting plate is disposed above the filtering chamber, and the active mechanism and the driven mechanism are disposed on the mounting plate; the exhaust type slurry storage device further includes a second frame The slurry chamber is disposed on the second frame.
- 根据权利要求4所述的蜂王浆过滤装置,其特征在于:所述抽真空排气机构包括与所述储浆室相连的排气管路以及与所述排气管路相连 的真空泵。A royal jelly filtering device according to claim 4, wherein said evacuation venting mechanism comprises an exhaust line connected to said slurry chamber and a vacuum pump connected to said exhaust line.
- 根据权利要求5所述的蜂王浆过滤装置,其特征在于:所述过滤网将所述过滤室分隔为上部除渣过滤分室和下部浆液存储分室,所述上部除渣过滤分室为矩形槽体结构,所述下部浆液存储分室为漏斗形结构;其中,所述下部浆液存储分室与所述储浆室之间通过浆液输送管路相连;在所述上部除渣过滤分室与所述下部浆液存储分室之间的结合处设有密封垫,所述过滤网设置在所述密封垫上。The apparatus for filtering royal jelly according to claim 5, wherein the filter screen divides the filter chamber into an upper slag filter compartment and a lower slurry storage compartment, and the upper slag filter compartment is a rectangular tank structure. The lower slurry storage compartment is a funnel-shaped structure; wherein the lower slurry storage compartment is connected to the slurry compartment through a slurry delivery line; and the upper slag filtration compartment and the lower slurry storage compartment A seal is provided at the junction, and the filter is disposed on the gasket.
- 根据权利要求6所述的蜂王浆过滤装置,其特征在于:所述上部除渣过滤分室中设有第一液位传感器,所述储浆室中设有第二液位传感器;设置在所述下部浆液存储分室出口处的所述浆液输送管路上设有第一控制阀,设置在所述储浆室进口处的所述浆液输送管路上设有第二控制阀,在所述排气管路上设有第三控制阀。The royal jelly filtering device according to claim 6, wherein a first liquid level sensor is disposed in the upper slag filtering sub-chamber, and a second liquid level sensor is disposed in the slurry storage chamber; a first control valve is disposed on the slurry delivery line at the outlet of the slurry storage compartment, and a second control valve is disposed on the slurry delivery line disposed at the inlet of the slurry storage chamber, and the exhaust gas pipeline is disposed on the exhaust gas pipeline There is a third control valve.
- 根据权利要求7所述的蜂王浆过滤装置,其特征在于:所述第二驱动机构包括与所述搅拌机构相连的减速电机;在所述储浆室的外部设有保温层。The apparatus for filtering royal jelly according to claim 7, wherein said second drive mechanism comprises a reduction motor coupled to said agitation mechanism; and an insulation layer is disposed outside said slurry storage chamber.
- 根据权利要求8所述的蜂王浆过滤装置,其特征在于:还包括控制装置,所述控制装置包括自动控制器,所述自动控制器分别与所述的伺服电机、减速电机、真空泵、第一液位传感器、第二液位传感器、第一控制阀、第二控制阀和第三控制阀相连。A royal jelly filtering device according to claim 8, further comprising control means, said control means comprising an automatic controller, said automatic controller and said servo motor, geared motor, vacuum pump, first liquid The position sensor, the second level sensor, the first control valve, the second control valve, and the third control valve are connected.
- 一种蜂王浆过滤方法,其特征在于:采用如权利要求9所述的蜂王浆过滤装置,具体包括如下步骤:A method for filtering a royal jelly, characterized in that the royal jelly filtering device according to claim 9 comprises the following steps:S1、在所述过滤室中安装所述过滤网,在所述过滤网上安装所述除渣机构,并调节所述除渣机构的压力达到预定要求,关闭所述第一控制阀;S1, installing the filter net in the filter chamber, installing the slag removing mechanism on the filter net, and adjusting the pressure of the slag removing mechanism to meet a predetermined requirement, and closing the first control valve;S2、将解冻后的蜂王浆加入所述过滤室中,确保所述过滤室中蜂王浆液位低于预定液位上限。S2, adding the thawed royal jelly to the filtering chamber to ensure that the liquid level of the royal jelly in the filtering chamber is lower than the upper limit of the predetermined liquid level.S3、接通电源,启动所述自动控制器,将所述除渣机构的运动速度设定为0.2~0.8m/s,将所述真空泵的真空压力设定为4~20kPa,将所述搅拌机构的搅拌速度设定为30~50rpm;S3, turning on the power, starting the automatic controller, setting the moving speed of the slag removing mechanism to 0.2-0.8 m/s, setting the vacuum pressure of the vacuum pump to 4-20 kPa, and stirring the The stirring speed of the mechanism is set to 30 to 50 rpm;S4、开启所述第一控制阀和所述第三控制阀,启动所述真空泵,当真空压力满足设定要求后,开启所述第二控制阀,启动所述伺服电机,所述 除渣机构进行自动过滤和除渣作业,并通过所述第一液位传感器实时监控所述过滤室中的蜂王浆液位;S4, the first control valve and the third control valve are opened, the vacuum pump is activated, and when the vacuum pressure meets the set requirement, the second control valve is opened to start the servo motor, and the slag removing mechanism Performing automatic filtration and slag removal operations, and monitoring the level of the royal jelly in the filtration chamber in real time by the first liquid level sensor;S5、当所述过滤室中的蜂王浆液位低于预定液位下限时,向所述过滤室中进行加液作业,当所述过滤室中的蜂王浆液位达到预定液位上限时,加液作业自动停止;S5. When the liquid level of the royal jelly in the filtering chamber is lower than the lower limit of the predetermined liquid level, the liquid adding operation is performed in the filtering chamber, and when the liquid level of the royal jelly in the filtering chamber reaches the upper limit of the predetermined liquid level, the liquid adding The job is automatically stopped;S6、当所述储浆室中的液位达到预定液位后,所述第二液位传感器传输启动信号,所述自动控制器启动所述减速电机,所述搅拌机构进行蜂王浆均质、脱气作业;S6. After the liquid level in the slurry storage chamber reaches a predetermined liquid level, the second liquid level sensor transmits a start signal, and the automatic controller activates the speed reduction motor, and the stirring mechanism performs homogenization and removal of the royal jelly. Gas operationS7、蜂王浆全部投入所述过滤室后,当所述过滤室中的蜂王浆液位低于预警液位时,所述第一液位传感器传输停止信号,所述自动控制器关闭所述第二控制阀,所述伺服电机停止工作,自动过滤和除渣作业完成;S7. After the royal jelly is all put into the filtering chamber, when the liquid level of the royal jelly in the filtering chamber is lower than the warning liquid level, the first liquid level sensor transmits a stop signal, and the automatic controller turns off the second control. Valve, the servo motor stops working, automatic filtering and slag removal operations are completed;S8、清理所述过滤室和所述浆液输送管路内残留的蜂王浆,并收集所述过滤网内的滤渣,完成清场作业。S8. Clean the residual royal jelly in the filter chamber and the slurry conveying pipeline, and collect the filter residue in the filter net to complete the clearing operation.
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Cited By (7)
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CN114504861A (en) * | 2022-04-20 | 2022-05-17 | 广东环凯生物科技有限公司 | On-site monitoring-free filtering control method and system |
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Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108096893B (en) * | 2017-12-27 | 2019-07-09 | 中国农业科学院蜜蜂研究所 | A kind of royal jelly filter device and method |
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB191313659A (en) * | 1912-06-12 | 1914-06-04 | Maschb Aktien Ges Balcke | Improvements in or relating to Cleaning Filters. |
CN203884605U (en) * | 2014-03-24 | 2014-10-22 | 钭礼俊 | Novel honey degassing and sterilizing tank |
CN205080654U (en) * | 2015-09-17 | 2016-03-09 | 深圳市祈飞科技有限公司 | Automatic squeeze juice and sell machine slagging -off mechanism and squeeze juice automatically and sell machine |
CN206596640U (en) * | 2017-02-23 | 2017-10-31 | 天津七七七科技发展有限公司 | A kind of special concentration purifying plant of honey |
CN206660693U (en) * | 2017-03-21 | 2017-11-24 | 青岛海佳机械有限公司 | A kind of waste water reclaiming device of water-jet loom |
CN108096893A (en) * | 2017-12-27 | 2018-06-01 | 中国农业科学院蜜蜂研究所 | A kind of royal jelly filter device and method |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54170478U (en) * | 1978-05-23 | 1979-12-01 | ||
US4731180A (en) * | 1983-08-03 | 1988-03-15 | Huff Karl C | Water-solids separator and wiper blade |
JPH061204Y2 (en) * | 1990-04-24 | 1994-01-12 | 中部スクリーン有限会社 | Screen cleaning device for separator |
JP3656044B2 (en) * | 2001-09-11 | 2005-06-02 | 喜久二 山口 | Method and apparatus for purifying royal jelly |
CN103039383B (en) * | 2013-01-21 | 2014-05-07 | 江西农业大学 | Integrated device for beewax cutting and jelly collecting for obtaining royal jelly |
CN206101516U (en) * | 2016-07-29 | 2017-04-19 | 青川县易诚电子商务有限责任公司 | Honey degassing tank |
CN207950802U (en) * | 2017-12-27 | 2018-10-12 | 中国农业科学院蜜蜂研究所 | A kind of royal jelly filter device |
-
2017
- 2017-12-27 CN CN201711447953.2A patent/CN108096893B/en active Active
-
2018
- 2018-06-07 WO PCT/CN2018/090283 patent/WO2019128114A1/en active Application Filing
- 2018-06-07 JP JP2020549846A patent/JP7008146B2/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB191313659A (en) * | 1912-06-12 | 1914-06-04 | Maschb Aktien Ges Balcke | Improvements in or relating to Cleaning Filters. |
CN203884605U (en) * | 2014-03-24 | 2014-10-22 | 钭礼俊 | Novel honey degassing and sterilizing tank |
CN205080654U (en) * | 2015-09-17 | 2016-03-09 | 深圳市祈飞科技有限公司 | Automatic squeeze juice and sell machine slagging -off mechanism and squeeze juice automatically and sell machine |
CN206596640U (en) * | 2017-02-23 | 2017-10-31 | 天津七七七科技发展有限公司 | A kind of special concentration purifying plant of honey |
CN206660693U (en) * | 2017-03-21 | 2017-11-24 | 青岛海佳机械有限公司 | A kind of waste water reclaiming device of water-jet loom |
CN108096893A (en) * | 2017-12-27 | 2018-06-01 | 中国农业科学院蜜蜂研究所 | A kind of royal jelly filter device and method |
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Also Published As
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CN108096893A (en) | 2018-06-01 |
CN108096893B (en) | 2019-07-09 |
JP7008146B2 (en) | 2022-01-25 |
JP2021505384A (en) | 2021-02-18 |
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