CN103639029B - Plant powder processing device - Google Patents
Plant powder processing device Download PDFInfo
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- CN103639029B CN103639029B CN201310678847.0A CN201310678847A CN103639029B CN 103639029 B CN103639029 B CN 103639029B CN 201310678847 A CN201310678847 A CN 201310678847A CN 103639029 B CN103639029 B CN 103639029B
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- plant
- drying box
- plant powder
- processing unit
- feeding auger
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- 238000009700 powder processing Methods 0.000 title abstract 4
- 238000001035 drying Methods 0.000 claims abstract description 59
- 239000000843 powder Substances 0.000 claims abstract description 24
- 238000010438 heat treatment Methods 0.000 claims abstract description 13
- 238000007599 discharging Methods 0.000 claims description 16
- 238000010298 pulverizing process Methods 0.000 claims description 8
- 235000013312 flour Nutrition 0.000 claims description 7
- 239000003507 refrigerant Substances 0.000 claims description 7
- 238000003801 milling Methods 0.000 claims description 6
- 230000008093 supporting effect Effects 0.000 claims description 5
- 238000009826 distribution Methods 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 11
- 238000004519 manufacturing process Methods 0.000 abstract description 10
- 238000000227 grinding Methods 0.000 abstract description 6
- 239000002826 coolant Substances 0.000 abstract 2
- 238000010924 continuous production Methods 0.000 abstract 1
- 239000000796 flavoring agent Substances 0.000 abstract 1
- 235000019634 flavors Nutrition 0.000 abstract 1
- 235000015097 nutrients Nutrition 0.000 abstract 1
- 239000000463 material Substances 0.000 description 16
- 241000196324 Embryophyta Species 0.000 description 15
- 230000005540 biological transmission Effects 0.000 description 14
- 235000003599 food sweetener Nutrition 0.000 description 6
- 239000003765 sweetening agent Substances 0.000 description 6
- 239000002131 composite material Substances 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- 235000013399 edible fruits Nutrition 0.000 description 3
- 238000007710 freezing Methods 0.000 description 3
- 230000008014 freezing Effects 0.000 description 3
- 230000033001 locomotion Effects 0.000 description 3
- 235000019640 taste Nutrition 0.000 description 3
- 240000000851 Vaccinium corymbosum Species 0.000 description 2
- 235000003095 Vaccinium corymbosum Nutrition 0.000 description 2
- 235000017537 Vaccinium myrtillus Nutrition 0.000 description 2
- 235000021014 blueberries Nutrition 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002372 labelling Methods 0.000 description 2
- 235000016709 nutrition Nutrition 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- UEDUENGHJMELGK-HYDKPPNVSA-N Stevioside Chemical compound O([C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@]12C(=C)C[C@@]3(C1)CC[C@@H]1[C@@](C)(CCC[C@]1([C@@H]3CC2)C)C(=O)O[C@H]1[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O1)O)[C@@H]1O[C@H](CO)[C@@H](O)[C@H](O)[C@H]1O UEDUENGHJMELGK-HYDKPPNVSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000019658 bitter taste Nutrition 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004108 freeze drying Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 229940013618 stevioside Drugs 0.000 description 1
- OHHNJQXIOPOJSC-UHFFFAOYSA-N stevioside Natural products CC1(CCCC2(C)C3(C)CCC4(CC3(CCC12C)CC4=C)OC5OC(CO)C(O)C(O)C5OC6OC(CO)C(O)C(O)C6O)C(=O)OC7OC(CO)C(O)C(O)C7O OHHNJQXIOPOJSC-UHFFFAOYSA-N 0.000 description 1
- 235000019202 steviosides Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The invention relates to a plant powder processing device. The plant powder processing device comprises a drying mechanism and a crushing mechanism, wherein the drying mechanism is communicated with the crushing mechanism through a corresponding pipeline; the drying mechanism comprises a drying box which is provided with a feeding port and can be vacuumized, a feeding auger which is vertically arranged along the feeding port of the drying box, a drying plate, a coolant pipe and a heating pipe, wherein the drying plate, the coolant pipe and the heating pipe are arranged in the drying box; the crushing mechanism comprises a crushing cavity, a lower grinding disc and an upper grinding disc, the lower grinding disc is arranged on the inner side bottom of the crushing cavity, and the upper grinding disc is connected to a position above the lower grinding disc in a rotating manner. The plant powder processing device has the advantages that the stream continuous production process requirements can be met, the production process is pollution-free, the plant powder processed by the device can maintain the original flavor and nutrients of plants, and the device is simpler in structure and low in cost.
Description
Technical field
The present invention relates to the grinding processing equipment of plant, particularly relate to a kind of processing unit (plant) of pure plant powder.
Background technology
In order to change the bitter taste of stevioside, applicant in this case designs a kind of fruity compound sweetener, and wherein used fruit powder, such as blueberry powder, therefore the production of sweetener relates to fructovegetative drying and powder process problem.
For dry, powder process, all there is independently equipment at present, its technical scheme is also open, but as these two kinds of cluster tool are got up to be used, the process requirements that sweetener is produced can not be reached, therefore the need of production of composite sweetener a kind of continuous-flow type continuous prodution and adapt to the corresponding device of certain output, and this equipment can keep the original nutritional labeling of fruit plant and peculiar taste in dry run, do not produce dust at pulverizing process energy continuous-flow type continuous seepage and affect production environment.
Summary of the invention
The object of the invention is to, provide and can adapt to needed for plant composite powder material manufacturing technique, a kind of preparation device of composite plant powder of such as, continuous-flow type continuous prodution needed for fruity compound sweetener production technology; The present invention also aims to a kind of preparation device of composite plant powder providing a kind of production process to pollute without powder.Its concrete technical scheme is as follows:
The processing unit (plant) of described pure plant powder, comprises drier and disintegrating mechanism, and described drier and disintegrating mechanism are by the mutual UNICOM of corresponding pipeline; Described drier comprises and is provided with charging aperture and the drying box of vacuum-pumping, the feeding auger vertically placed along described drying box charging aperture and the drying plate, refrigerant pipe and the heating tube that are placed in drying box; The lower millstone that described disintegrating mechanism comprises a pulverizing cavity, be placed in described pulverizing cavity inside bottom and the upper millstone be rotatably connected on above described lower millstone.
Described drying box charging aperture arranges feed hopper, and described feed hopper is provided with support, and described feeding auger is supported on support by least two place's bearings on described support and can moves up and down along supporting place; Drying box sidewall is provided with the aspirating hole be communicated with the air exhauster vacuumized and the air admission hole be communicated with air compressor machine.
Described drier also comprises a driving-chain, drive sleeve unit and moves axially gear unit; Described drive sleeve unit comprises drive sleeve and bearing, and close-fitting is in the rotating shaft of feeding auger and in the corresponding endoporus of described drive sleeve list respectively for the Internal and external cycle of described bearing, and drive sleeve is connected with the described gear unit that moves axially.
The described gear unit that moves axially is a crank connecting link gear unit, and described crank connecting link gear unit comprises crank and connecting rod, drive sleeve and described crank hinged; Described driving-chain comprises driving pair and driven pair, and described driven pair is connected in the rotating shaft of feeding auger.
The described gear unit that moves axially is a crank connecting link gear unit, and described crank connecting link gear unit comprises crank and connecting rod, drive sleeve and described crank hinged; Described driving-chain comprises driving pair and driven pair, and described driven pair is connected in the rotating shaft of feeding auger.
Described drying plate has some layers, is centered around feeding auger week side along the axial distribution of described feeding auger in drying box, and each dry plate is established somely has passage.
Described refrigerant pipe and heating tube are distributed on every layer of drying plate and are also connected with corresponding compressor and heating power supply respectively.
Discharging opening is provided with facing to feeding auger end bottom described drying box, discharge outlet is provided with discharge valve, described discharge valve comprises valve seat and spool, valve core rotation is connected to valve seat, the circumference of valve seat and spool is respectively equipped with uniform discharging opening, spool two described in form striker plate between discharging opening.
The flour milling of described upper millstone is a conical surface, and the conical surface is provided with the pusher groove formed by the helicoid of two handing-over, and the groove width of described pusher groove is narrowed gradually to center.
The center of described lower millstone is provided with the discharge opening for discharging.
Beneficial effect of the present invention is, can realize continuous-flow type continuous seepage that is dry and powder process, meet the manufacturing technique requirent of composite sweetener, equipment is succinct, and cost is low; And: the taste that dry run can keep former plant to have and nutritional labeling, simultaneously fast dry; Crushing process adopts and grinds mode energy continuous-flow type continuous prodution, more adapts to fructovegetative characteristic and makes crushing process continuous, being convenient to the production of continuous-flow type, and there will not be the situation of dust polluting environment.
Accompanying drawing explanation
Fig. 1 is the structural representation of preparation device of the present invention.
Fig. 2 is the top view of the device of preparation shown in Fig. 1.
Fig. 3 is the structural representation of drier.
Fig. 4 is the B-B sectional view of drying machine shown in Fig. 3
Fig. 5 is the structural representation of drive sleeve unit.
Fig. 6 is the structural representation moving axially gear unit formed by sprocket chain bar.
Fig. 7 is the structural representation of auger supporting seat.
Fig. 8 is the structural representation of the discharge valve of drying box bottom discharge mouth.
Fig. 9 is the C-C face sectional view of valve shown in Fig. 8.
Figure 10 is the structural representation of disintegrating mechanism.
Figure 11 is the structural representation of lower millstone.
Figure 12 is the structural representation of upper millstone.
Figure 13 is the A-A face sectional view of upper millstone shown in Figure 12.
as Fig. 1,2, preparation device of the present invention has a drier 1, and drier 1 lower end connects the disintegrating mechanism 2 of below by pipeline 4, and the below of disintegrating mechanism 2 arranges mixed organization 3, and both are communicated with by pipeline 4.
Above-mentioned drier 1 can see Fig. 3,4, and have a circular drying box 110, drying box upper end is provided with upper cover 105, this upper cover 105 is provided with charging aperture, charging aperture upper end connects a hopper 106, and arranges support 103 on hopper 106, and support 103 is for supporting feeding auger 104.Therefore, two corresponding positions on support 103 arrange bearing block 117 respectively, and certain supporting-point is not limited to 2 places, can increase more supporting-point for increasing feeding auger 104 rigidity.Feeding auger 104 is by the pulley transmission mechanism transmission comprised, drive pulley 103, driven belt pulley 102 and belt 101 form, and wherein driven belt pulley 102 is connected in the rotating shaft of feeding auger 104.Feeding auger 104 rotates under above-mentioned pulley transmission mechanism transmission, and the crank connecting link gear unit be made up of crank 501 and connecting rod 502 drives feeding auger 104 to do axial movement, wherein crank 501 is driven by the stepper motor 505 of correspondence, and connecting rod 502 is connected with the rotating shaft of feeding auger 104 by drive sleeve unit 503.
As Fig. 5, drive sleeve unit 503 has drive sleeve 5031 and bearing 5032, and bearing 5032 is by inner ring close-fitting on feeding auger 104, and its outer ring close-fitting is in the endoporus of drive sleeve 5031, like this under pulley transmission mechanism transmission, the rotation needed for feeding auger 104 can be realized and move axially.
Certainly, the transmission of feeding auger 104 is not limited to the corresponding transmission of above-mentioned pulley transmission mechanism and crank connecting link gear unit, such as, sprocket wheel chain-driving feeding auger 104 also can be adopted to rotate; Feeding auger 104 is driven to axially move with the rack pinion unit with the formation of gear 602, tooth bar 601 and Connection Block 603 as shown in Figure 6.Connection Block 603 in this gear unit is connected in the drive sleeve 5031 of above-mentioned drive sleeve unit 503, and is connected on Connection Block 603 by tooth bar 601.Moving axially of feeding auger 104, is rotated by gear 602 and gear 602 realizes with the engaged transmission of tooth bar 601.
For adapting to the motion of feeding auger 104, the setting of the bearing block 117 of two supportings place is as Fig. 7, and feeding auger 104 is bearing on axle sleeve 1142 by bearing 1411, and axle sleeve 1142 is slidably connected to bearing block 117.
Drying box 110 inner chamber arranges five layers of drying plate 112 by axial direction, and drying plate 112, in annular, be which is provided with passage 117, is fixed on the inner chamber of drying box by drying plate support 113.Be distributed with refrigerant pipe 108 and heating tube 109 in the downside of every layer of drying plate 112, wherein refrigerant pipe 108 circularizes distribution.Refrigerant pipe 108 is connected with the refrigeration machine be arranged on outside drying box 110 and heating power supply respectively with heating tube 109.In order to make moisture in material produce the solid-state distillation to liquid in freeze drying, drying box 110 is connected with vavuum pump 118 by corresponding aspirating hole (not shown).
Drying box 110 bottom centre position is provided with discharging opening, so that dried material is discharged.The opening and closing of discharging opening is completed by the discharge valve 115 being arranged on discharge outlet, and see Fig. 8,9, discharge valve 115 forms primarily of valve seat 1151 and spool 1152 and driven by stepper motor 114.Valve seat 1151 is fixedly connected on the described discharge outlet bottom drying box 110, spool 1152 is sheathed on inside valve seat 1151 and also can rotates by opposite valve seat 1151, the circumference of valve seat and spool is respectively equipped with identical and uniform several discharging openings 11511, 11521, backgauge face 11522 is formed between two discharging openings of spool, valve closing be spool under driven by motor, turn on backgauge face 11522 positive alignment valve seat discharging opening 11511 time position, all valve open state when backgauge face 11522 is not in and aims at valve seat top discharge mouth 11511 position, when discharging opening 11511 is not blocked in backgauge face 11522 completely, valve is in maximum open mode.
Discharge for the ease of the material in drying box 110, be provided with the air admission hole 107 entered for pressed gas at the sidewall of drying box 110, air compressor machine 121 is connected with this pore 107 by corresponding pipeline.
Feeding auger 104 is placed in the center of annular drying plate, makes drying plate be centered around feeding auger week side.Under pulley transmission mechanism transmission, feeding auger 104 rotates while move down, and is from top to bottom delivered on each layer drying plate 112 by the material in hopper.The position corresponding to discharging opening on the downside of the cover plate 105 of drying box 110 upper end is provided with sealed door 111, and this sealed door 111 is plugged on cover plate 105.After having sent material, transmission feeding auger 104 has rotated backward by described pulley transmission mechanism, and feeding auger 104 moves up, and shifts out drying box 110, and sealed door 111 closes.
For the ease of the drying of material, above-mentioned drying plate is arranged some passages 117, a kind of preferred scheme is that passage distributes ringwise.
As Figure 10, disintegrating mechanism 2 has a pulverizing cavity 208, the bottom of this pulverizing cavity 205 arranges a lower millstone 205, see Figure 11, the center of lower millstone 205 is provided with flour opening 2051, one upper millstone 204 corresponding to lower millstone 205 is placed in the top of lower millstone 205 and is rotationally connected with on mill support 203, mill Bracket setting in pulverizing cavity 208 side, see figure, 12,13.
The mill pressure space between upper lower millstone is entered for ease of material to be comminuted, the flour milling 2041 of upper millstone 204 is designed to the conical surface of a slightly tapering, about 2-5 degree, and pusher groove 2041 is set on flour milling, the groove sidewall of this pusher groove is formed by the helicoid 2042 of two handing-over, the groove width of pusher groove 2041 is narrowed gradually, until join the center in mill 204 to center.Such material constantly pushes mill center under the effect of pusher groove groove sidewall, and due to the flour milling 2041 of upper millstone be band tapering, in the process to central motion, the spacing of two mills reduces gradually, material is crushed broken by mill, form powder, discharged by the flour opening at lower millstone 205 center.
During apparatus of the present invention work, have driven pulley 102, belt 101 belt pulley drive unit driving under drive feeding auger 104 to rotate, delivered on each layer drying plate 112 by plant material in hopper 106, material paves on drying plate 112, completes charging.After having feeded, feeding auger 104 moves up under the drive of crank connecting link gear unit 5 or rack pinion unit 6, leave drying box 110, the sealed door 111 of drying box upper end is closed, refrigeration machine 119 is opened, plant material in drying box is carried out below freezing freezing, after freezing end, open vavuum pump 118 to vacuumize, heating power supply 120 pairs of heating tube energisings, make dry the temperature inside the box a little more than room temperature, after drying terminates, valve 115 is opened, air compressor machine 121 is opened and enters drying box 110 inner chamber by air admission hole 107 simultaneously, discharge under help is blown compressed-air actuated.
Dried material enters the lower millstone 205 of disintegrating mechanism 2 through pipeline 4, belt 201 drives belt pulley 202 to rotate thus drives upper millstone 204 to rotate, material is brought into the district that mills and is milled by the helicla flute on upper millstone 204, and the material after milling is exported by the discharging opening of lower millstone.
Through the fruit plant of apparatus of the present invention process, such as blueberry can keep distinctive taste preferably, and whole manufacturing process can realize the continuous prodution of flowing water.
Claims (10)
1. a processing unit (plant) for pure plant powder, is characterized in that comprising drier and disintegrating mechanism, and described drier and disintegrating mechanism are by the mutual UNICOM of corresponding pipeline; Described drier comprises and is provided with charging aperture and the drying box of vacuum-pumping, the feeding auger vertically placed along described drying box charging aperture and the drying plate, refrigerant pipe and the heating tube that are placed in drying box; The lower millstone that described disintegrating mechanism comprises a pulverizing cavity, be placed in described pulverizing cavity inside bottom and the upper millstone be rotatably connected on above described lower millstone.
2. the processing unit (plant) of a kind of pure plant powder according to claim 1, it is characterized in that described drying box charging aperture arranges feed hopper, described feed hopper is provided with support, and described feeding auger is supported on support by least two place's bearings on described support and can moves up and down along supporting place; Drying box sidewall is provided with the aspirating hole be communicated with the air exhauster vacuumized and the air admission hole be communicated with air compressor machine.
3. the processing unit (plant) of a kind of pure plant powder according to claim 1 and 2, is characterized in that described drier also comprises a driving-chain, drive sleeve unit and moves axially gear unit; Described drive sleeve unit comprises drive sleeve and bearing, and close-fitting is in the rotating shaft of feeding auger and in the corresponding endoporus of described drive sleeve list respectively for the Internal and external cycle of described bearing, and drive sleeve is connected with the described gear unit that moves axially.
4. the processing unit (plant) of a kind of pure plant powder according to claim 3, moving axially gear unit described in it is characterized in that is a crank connecting link gear unit, and described crank connecting link gear unit comprises crank and connecting rod, drive sleeve and described crank hinged; Described driving-chain comprises driving pair and driven pair, and described driven pair is connected in the rotating shaft of feeding auger.
5. the processing unit (plant) of a kind of pure plant powder according to claim 3, moving axially gear unit described in it is characterized in that is a rack pinion unit, described rack pinion unit comprises pitch wheel, tooth bar and Connection Block, described Connection Block is connected in the drive sleeve of described drive sleeve unit, and tooth bar is on Connection Block.
6. the processing unit (plant) of a kind of pure plant powder according to claim 4, is characterized in that described drying plate has some layers, is centered around feeding auger week side along the axial distribution of described feeding auger in drying box, and each dry plate is established somely has passage.
7. the processing unit (plant) of a kind of pure plant powder according to claim 5, is characterized in that described refrigerant pipe and heating tube are distributed on every layer of drying plate and is also connected with corresponding compressor and heating power supply respectively.
8. the processing unit (plant) of a kind of pure plant powder according to claim 1, it is characterized in that being provided with discharging opening facing to feeding auger end bottom described drying box, discharge outlet is provided with discharge valve, described discharge valve comprises valve seat and spool, valve core rotation is connected to valve seat, the circumference of valve seat and spool is respectively equipped with uniform discharging opening, spool two described in form striker plate between discharging opening.
9. the processing unit (plant) of a kind of pure plant powder according to claim 1, is characterized in that the flour milling of described upper millstone is a conical surface, and the conical surface is provided with the pusher groove formed by the helicoid of two handing-over, and the groove width of described pusher groove is narrowed gradually to center.
10. the processing unit (plant) of a kind of pure plant powder according to claim 1 or 7, is characterized in that the center of described lower millstone is provided with the discharge opening for discharging.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310678847.0A CN103639029B (en) | 2013-12-14 | 2013-12-14 | Plant powder processing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310678847.0A CN103639029B (en) | 2013-12-14 | 2013-12-14 | Plant powder processing device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103639029A CN103639029A (en) | 2014-03-19 |
| CN103639029B true CN103639029B (en) | 2015-06-17 |
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| CN201310678847.0A Active CN103639029B (en) | 2013-12-14 | 2013-12-14 | Plant powder processing device |
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| CN (1) | CN103639029B (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104148321B (en) * | 2014-09-08 | 2015-12-23 | 程梅雪 | Concentrating type literary composition Concha Meretricis Seu Cyclinae powder process equipment |
| CN104223114B (en) * | 2014-09-08 | 2015-10-14 | 程梅雪 | Continuous-flow type clam shell system of processing |
| CN104146268B (en) * | 2014-09-08 | 2015-08-05 | 程梅雪 | The cleaning of clam shell, pulverizing, dry continuous-flow type device |
| CN104668074B (en) * | 2015-02-17 | 2017-04-05 | 无锡昊瑜节能环保设备有限公司 | A kind of coal dust exsiccator |
| CN106196949B (en) * | 2016-08-30 | 2018-10-16 | 兴化格林生物制品有限公司 | The processing unit (plant) of stevioside fruit powder |
| CN106196975B (en) * | 2016-08-30 | 2018-10-16 | 兴化格林生物制品有限公司 | The drying device of stevioside fruit powder |
| CN106391200B (en) * | 2016-08-30 | 2020-04-07 | 兴化格林生物制品有限公司 | Stevia rebaudianum candy powder crushing mechanism |
| CN106195394B (en) * | 2016-08-30 | 2018-10-16 | 兴化格林生物制品有限公司 | Valve mechanism for the processing of stevioside fruit powder |
| CN109907667B (en) * | 2017-03-21 | 2022-07-29 | 威海参威电子科技有限责任公司 | Household multifunctional soybean milk machine |
| CN109758000B (en) * | 2017-03-21 | 2022-08-12 | 威海迅捷智能科技有限公司 | Multifunctional household soybean milk machine |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4169979B2 (en) * | 2002-01-11 | 2008-10-22 | 三井造船株式会社 | Solid waste disposal equipment |
| CN2732461Y (en) * | 2004-11-04 | 2005-10-12 | 礼兴塑胶（深圳）有限公司 | Integrated machine for disintegrating, mixing and drying |
| CN2823935Y (en) * | 2005-07-14 | 2006-10-04 | 赵财祥 | Rotary drum type concentrating crushing vacuum drier |
| CN203336917U (en) * | 2013-05-10 | 2013-12-11 | 安徽宝芝堂药业有限公司 | Rotation type drying device for traditional Chinese medicine micro powder |
| CN203874871U (en) * | 2013-12-14 | 2014-10-15 | 周伯雅 | Processing device for plant powder |
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Effective date of registration: 20170428 Address after: Xinghua City, Jiangsu province 225700 city of Taizhou Economic Development Zone Road No. 26 Patentee after: Xinghua Green Biological Preparation Co., Ltd. Address before: 225776 Jiangsu city of Taizhou province Xinghua Economic Development Zone on Fu Road No. 26 Patentee before: Zhou Boya |