CN204897573U - Sulfuric acid monohydrate zinc waste water processing system - Google Patents
Sulfuric acid monohydrate zinc waste water processing system Download PDFInfo
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- CN204897573U CN204897573U CN201520515496.6U CN201520515496U CN204897573U CN 204897573 U CN204897573 U CN 204897573U CN 201520515496 U CN201520515496 U CN 201520515496U CN 204897573 U CN204897573 U CN 204897573U
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- 239000002351 wastewater Substances 0.000 title abstract description 13
- MZNYADCLSDCSHV-UHFFFAOYSA-N sulfuric acid;zinc;hydrate Chemical compound O.[Zn].OS(O)(=O)=O MZNYADCLSDCSHV-UHFFFAOYSA-N 0.000 title abstract 3
- 238000006243 chemical reaction Methods 0.000 claims abstract description 128
- 238000010517 secondary reaction Methods 0.000 claims abstract description 47
- 239000012530 fluid Substances 0.000 claims abstract description 38
- 238000004519 manufacturing process Methods 0.000 claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 18
- RNZCSKGULNFAMC-UHFFFAOYSA-L zinc;hydrogen sulfate;hydroxide Chemical compound O.[Zn+2].[O-]S([O-])(=O)=O RNZCSKGULNFAMC-UHFFFAOYSA-L 0.000 claims description 23
- 238000004065 wastewater treatment Methods 0.000 claims description 21
- 239000002244 precipitate Substances 0.000 claims description 18
- 238000003756 stirring Methods 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 239000012141 concentrate Substances 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 238000004062 sedimentation Methods 0.000 abstract 4
- -1 former liquid bath Chemical compound 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000008520 organization Effects 0.000 description 2
- 239000001828 Gelatine Substances 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- 241000607479 Yersinia pestis Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052716 thallium Inorganic materials 0.000 description 1
- BKVIYDNLLOSFOA-UHFFFAOYSA-N thallium Chemical compound [Tl] BKVIYDNLLOSFOA-UHFFFAOYSA-N 0.000 description 1
- 150000003751 zinc Chemical class 0.000 description 1
Landscapes
- Removal Of Specific Substances (AREA)
Abstract
The utility model provides a can be effectively carry out the sulfuric acid monohydrate zinc waste water processing system that handle and structural design reasonable to the waste water that produces in the production of sulfuric acid monohydrate zinc, including former liquid bath, via former liquid pump with former liquid bath corresponds the elementary pressure filter of intercommunication, it still include primary reaction pond unit, with the liquid outlet of primary reaction pond unit correspond the intercommunication elementary sedimentation tank, with the leakage fluid dram of elementary sedimentation tank correspond the intercommunication secondary reaction pond unit and with the liquid outlet of secondary reaction pond unit corresponds the secondary sedimentation tank of intercommunication, still include with the leakage fluid dram of secondary sedimentation tank corresponds the secondary pressure filter of intercommunication, the leakage fluid dram of secondary pressure filter still with the inlet of primary reaction pond unit corresponds the intercommunication, the inlet of primary reaction pond unit still with the leakage fluid dram of elementary pressure filter corresponds the intercommunication, primary reaction pond unit and secondary reaction pond unit all include four serial connectivity's reaction tank.
Description
Technical field
The utility model relates to a kind of Waste Water Treatment, particularly relates to a kind of Zinc Sulphate Monohydrate production wastewater treatment system.
Background technology
At present; Zinc Sulphate Monohydrate has been widely used in fodder additives, chemical industry, national defence, fertilizer, ore dressing, pharmacy, rubber, electronics, printing and dyeing agent, gelatine finings and protective material, has electroplated, has prevented the field such as fruit tree diseases and pests and circulating water cooling treatment, viscose fiber and nylon fiber, is also the raw material manufacturing zinc salt and lithopone.Therefore Zinc Sulphate Monohydrate plays an important role in China's economic construction, current Zinc Sulphate Monohydrate is all multiple operation aborning, wherein highly energy-consuming may be related to, the problem of high pollution, and under current economic circumstances, highly energy-consuming, the enterprise of high pollution is not suitable with expanding economy, do not meet the policy of the relevant energy-saving and emission-reduction of country simultaneously yet, highly energy-consuming simultaneously, high pollution also can increase the cost of enterprise, destroy the environment of periphery, such as in Zinc Sulphate Monohydrate is produced, a lot of trade effluent can be produced, these waste water comprise plant effluent, in factory effluent, and containing heavy metal in the waste water produced in Zinc Sulphate Monohydrate is produced, such as cadmium, thallium etc., therefore this type of waste water can not arbitrarily discharge, just can discharge after needing to process its waste water, in currently available technology, this type of waste water is because of handling procedure complexity, high in cost of production reason, a lot of enterprise can not meet emission standard to this type of wastewater treatment, also can affect the problems such as periphery soil and water resources, therefore, be necessary to be solved the problems referred to above.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, adapts to reality need, provides that the waste water produced in a kind of can effectively production Zinc Sulphate Monohydrate processes and the Zinc Sulphate Monohydrate production wastewater treatment system of reasonable in design.
In order to realize the purpose of this utility model, the technical scheme that the utility model adopts is:
Design a kind of Zinc Sulphate Monohydrate production wastewater treatment system, comprise stoste pond, via the concentrate pump elementary pressure filter that be communicated with corresponding to described stoste pond; It also comprise primary reaction pool unit, corresponding with the liquid outlet of described primary reaction pool unit be communicated with primary clarifier, with the corresponding secondary reaction pool unit that is communicated with of the leakage fluid dram of described primary clarifier and the post-precipitate pond that be communicated with corresponding to the liquid outlet of described secondary reaction pool unit, also comprise the secondary pressure filter that be communicated with corresponding to the leakage fluid dram in described post-precipitate pond, the leakage fluid dram of described secondary pressure filter is also corresponding with the fluid inlet of described primary reaction pool unit to be communicated with; The fluid inlet of described primary reaction pool unit is also corresponding with the leakage fluid dram of described elementary pressure filter to be communicated with; Described primary reaction pool unit and secondary reaction pool unit include the reaction tank of four serial communication.
Further, four reaction tanks in described primary reaction pool unit and four reaction tanks in secondary reaction pool unit all linearly shape are arranged, and the middle and upper part sidewall of adjacent two reaction tanks on the middle and upper part sidewall of adjacent two reaction tanks in primary reaction pool unit and in secondary reaction pool unit all offers a liquid outlet, in primary reaction pool unit and secondary reaction pool unit, adjacent two reaction tanks are communicated with via the liquid outlet on reaction tank, and the middle and upper part sidewall being in two the 4th reaction tanks of tail end in primary reaction pool unit and secondary reaction pool unit all offers leakage fluid dram, the leakage fluid dram be in described primary reaction pool unit on the 4th reaction tank of tail end is communicated with via pipeline is corresponding with the fluid inlet of described primary clarifier, the leakage fluid dram be in described secondary reaction pool unit on the 4th reaction tank of tail end is communicated with via pipeline is corresponding with the fluid inlet in described post-precipitate pond.
Further, also comprise the working shaft be communicated with water source, described working shaft is also corresponding with the first reaction tank be in described primary reaction pool unit to be foremost communicated with.
Further, be provided with stirring arm in four reaction tanks in four reaction tanks in described primary reaction pool unit and in secondary reaction pool unit, described stirring rake is pusher stirring rake.
Further, above four reaction tanks above four reaction tanks in described primary reaction pool unit on Chi Kou and in secondary reaction pool unit, Chi Kou is provided with supporting network.
Further, described elementary pressure filter is also communicated with via the first transferpump is corresponding with the first reaction tank being positioned at front end in described primary reaction pool unit.
Further, the 4th reaction tank being positioned at tail end in described primary reaction pool unit is communicated with via the second transferpump is corresponding with described primary clarifier.
Further, described primary clarifier is communicated with via the 3rd transferpump is corresponding with the first reaction tank being positioned at front end in described secondary reaction pool unit.
Further, the 4th reaction tank being positioned at tail end in described secondary reaction pool unit is communicated with via the 4th transferpump is corresponding with described post-precipitate pond.
Further, described post-precipitate pond is communicated with via the 5th transferpump is corresponding with described secondary pressure filter.
The beneficial effects of the utility model are:
1. effectively can be processed Zinc Sulphate Monohydrate factory effluent by native system, the concrete emulsification, catalytic treatment etc. can carrying out repeatedly via the primary reaction pool unit of the design and secondary reaction pool unit, and via elementary pressure filter, secondary pressure filter and primary clarifier and post-precipitate pond, its throw out is processed, reach the purifying treatment to greatest extent to wastewater treatment, made its waste water meet emission standard after treatment.
2. the design is when wastewater treatment, and its waste water can be passed through and recycles, and to reduce the use to water resources, reduces the input cost of enterprise.
3. the design is rational in infrastructure compact, is applicable to enterprise's serialization water treatment work.
4. the utility model also has other advantages, will propose in the lump with corresponding structure in an embodiment.
Accompanying drawing explanation
Fig. 1 is cardinal principle schematic diagram of the present utility model;
Fig. 2 is four reaction tank primary structures in the utility model in primary reaction pool unit and mutually arranges relation schematic diagram;
In figure: 1. stoste pond; 2. concentrate pump; 3. elementary pressure filter; 4. the first transferpump; 5. working shaft; 6. the first reaction tank in primary reaction pool unit; 7. the second reaction tank in primary reaction pool unit; 8. the 3rd reaction tank in primary reaction pool unit; 9. the 4th reaction tank in primary reaction pool unit; 10. the second transferpump; 11. primary clarifier; 12. the 3rd transferpumps; The first reaction tank in 13. secondary reaction pool units; The second reaction tank in 14. secondary reaction pool units; The 3rd reaction tank in 15. secondary reaction pool units; The 4th reaction tank in 16. secondary reaction pool units; 17. the 4th transferpumps; 18. post-precipitate ponds; 19. the 5th transferpumps; 20. level pressure filter; 21,22. stirring arms; 23,24. supporting networks; 25,26. liquid outlets; 27. leakage fluid drams.
Embodiment
Below in conjunction with drawings and Examples, the utility model is further illustrated:
Embodiment 1: a kind of Zinc Sulphate Monohydrate production wastewater treatment system, see Fig. 1, Fig. 2; It comprises stoste pond, via the concentrate pump elementary pressure filter that be communicated with corresponding to described stoste pond; It also comprise primary reaction pool unit, corresponding with the liquid outlet of described primary reaction pool unit be communicated with primary clarifier, with the corresponding secondary reaction pool unit that is communicated with of the leakage fluid dram of described primary clarifier and the post-precipitate pond that be communicated with corresponding to the liquid outlet of described secondary reaction pool unit, also comprise the secondary pressure filter that be communicated with corresponding to the leakage fluid dram in described post-precipitate pond, the leakage fluid dram of described secondary pressure filter is also corresponding with the fluid inlet of described primary reaction pool unit to be communicated with; The fluid inlet of described primary reaction pool unit is also corresponding with the leakage fluid dram of described elementary pressure filter to be communicated with; Described primary reaction pool unit and secondary reaction pool unit include the reaction tank of four serial communication.Concrete, shown in Figure 2, the primary structure schematic diagram of the design's only picture primary reaction pool unit, the primary reaction pool unit of the design and secondary reaction pool unit project organization and principle similar, therefore secondary reaction pool unit project organization and principle do not draw corresponding view, as figure, four reaction tanks 6 in described primary reaction pool unit, 7, 8, 9 and secondary reaction pool unit in four reaction tanks 13, 14, 15, 16 all linearly shape settings, and adjacent two reaction tanks 6 in primary reaction pool unit, the middle and upper part sidewall of adjacent two reaction tanks on the middle and upper part sidewall of 7 and in secondary reaction pool unit all offers a liquid outlet 25, 26, in primary reaction pool unit and secondary reaction pool unit, adjacent two reaction tanks 6, 7 via reaction tank 6, liquid outlet 25 on 7, 26 are communicated with, and the middle and upper part sidewall being in two the 4th reaction tanks of tail end in primary reaction pool unit and secondary reaction pool unit all offers leakage fluid dram 27, the leakage fluid dram 27 be in described primary reaction pool unit on the 4th reaction tank of tail end is communicated with via pipeline is corresponding with the fluid inlet of described primary clarifier 11, the leakage fluid dram be in described secondary reaction pool unit on the 4th reaction tank 16 of tail end is communicated with via pipeline is corresponding with the fluid inlet in described post-precipitate pond 18.
Further, in order to efficiency operation and the stability of native system, native system also comprises the working shaft 5 be communicated with water source, and described working shaft 5 is also corresponding with the first reaction tank 6 be in described primary reaction pool unit to be foremost communicated with.Further, be provided with stirring arm 21,22 in four reaction tanks in four reaction tanks 6,7,8,9 in described primary reaction pool unit and in secondary reaction pool unit, described stirring rake is pusher stirring rake.Further, above four reaction tanks above four reaction tanks in described primary reaction pool unit on Chi Kou and in secondary reaction pool unit, Chi Kou is provided with supporting network 23,24, this supporting network can impel staff to stand on corresponding reaction tank, so that staff checks the situation in reaction tank.In native system, described elementary pressure filter is also communicated with via the first transferpump 4 is corresponding with the first reaction tank 6 being positioned at front end in described primary reaction pool unit.The 4th reaction tank 9 being positioned at tail end in described primary reaction pool unit is communicated with via the second transferpump 10 is corresponding with described primary clarifier 11.Described primary clarifier 11 is communicated with via the 3rd transferpump 12 is corresponding with the first reaction tank 13 being positioned at front end in described secondary reaction pool unit.The 4th reaction tank 16 being positioned at tail end in described secondary reaction pool unit is communicated with via the 4th transferpump 17 is corresponding with described post-precipitate pond 18.Described post-precipitate pond 18 is communicated with via the 5th transferpump 19 is corresponding with described secondary pressure filter.
To sum up, effectively can be processed Zinc Sulphate Monohydrate factory effluent by native system, the concrete emulsification, catalytic treatment etc. can carrying out repeatedly via the primary reaction pool unit of the design and secondary reaction pool unit, and via elementary pressure filter, secondary pressure filter and primary clarifier and post-precipitate pond, its throw out is processed, reach the purifying treatment to greatest extent to wastewater treatment, made its waste water meet emission standard after treatment.Meanwhile, the design is when wastewater treatment, and its waste water can be passed through and recycles, and to reduce the use to water resources, reduces the input cost of enterprise.
What embodiment of the present utility model was announced is preferred embodiment; but be not limited thereto; those of ordinary skill in the art; very easily according to above-described embodiment; understand spirit of the present utility model; and make different amplifications and change, but only otherwise depart from spirit of the present utility model, all in protection domain of the present utility model.
Claims (10)
1. a Zinc Sulphate Monohydrate production wastewater treatment system, comprises stoste pond, via the concentrate pump elementary pressure filter that be communicated with corresponding to described stoste pond; It is characterized in that: it also comprise primary reaction pool unit, corresponding with the liquid outlet of described primary reaction pool unit be communicated with primary clarifier, with the corresponding secondary reaction pool unit that is communicated with of the leakage fluid dram of described primary clarifier and the post-precipitate pond that be communicated with corresponding to the liquid outlet of described secondary reaction pool unit, also comprise the secondary pressure filter that be communicated with corresponding to the leakage fluid dram in described post-precipitate pond, the leakage fluid dram of described secondary pressure filter is also corresponding with the fluid inlet of described primary reaction pool unit to be communicated with; The fluid inlet of described primary reaction pool unit is also corresponding with the leakage fluid dram of described elementary pressure filter to be communicated with; Described primary reaction pool unit and secondary reaction pool unit include the reaction tank of four serial communication.
2. Zinc Sulphate Monohydrate production wastewater treatment system as claimed in claim 1, it is characterized in that: four reaction tanks in described primary reaction pool unit and four reaction tanks in secondary reaction pool unit all linearly shape are arranged, and the middle and upper part sidewall of adjacent two reaction tanks on the middle and upper part sidewall of adjacent two reaction tanks in primary reaction pool unit and in secondary reaction pool unit all offers a liquid outlet, in primary reaction pool unit and secondary reaction pool unit, adjacent two reaction tanks are communicated with via the liquid outlet on reaction tank, and the middle and upper part sidewall being in two the 4th reaction tanks of tail end in primary reaction pool unit and secondary reaction pool unit all offers leakage fluid dram, the leakage fluid dram be in described primary reaction pool unit on the 4th reaction tank of tail end is communicated with via pipeline is corresponding with the fluid inlet of described primary clarifier, the leakage fluid dram be in described secondary reaction pool unit on the 4th reaction tank of tail end is communicated with via pipeline is corresponding with the fluid inlet in described post-precipitate pond.
3. Zinc Sulphate Monohydrate production wastewater treatment system as claimed in claim 2, it is characterized in that: also comprise the working shaft be communicated with water source, described working shaft is also corresponding with the first reaction tank be in described primary reaction pool unit to be foremost communicated with.
4. Zinc Sulphate Monohydrate production wastewater treatment system as claimed in claim 2, it is characterized in that: be provided with stirring arm in four reaction tanks in four reaction tanks in described primary reaction pool unit and in secondary reaction pool unit, described stirring rake is pusher stirring rake.
5. Zinc Sulphate Monohydrate production wastewater treatment system as claimed in claim 2, is characterized in that: above four reaction tanks above four reaction tanks in described primary reaction pool unit on Chi Kou and in secondary reaction pool unit, Chi Kou is provided with supporting network.
6. Zinc Sulphate Monohydrate production wastewater treatment system as claimed in claim 2, is characterized in that: described elementary pressure filter is also communicated with via the first transferpump is corresponding with the first reaction tank being positioned at front end in described primary reaction pool unit.
7. Zinc Sulphate Monohydrate production wastewater treatment system as claimed in claim 2, is characterized in that: the 4th reaction tank being positioned at tail end in described primary reaction pool unit is communicated with via the second transferpump is corresponding with described primary clarifier.
8. Zinc Sulphate Monohydrate production wastewater treatment system as claimed in claim 2, is characterized in that: described primary clarifier is communicated with via the 3rd transferpump is corresponding with the first reaction tank being positioned at front end in described secondary reaction pool unit.
9. Zinc Sulphate Monohydrate production wastewater treatment system as claimed in claim 2, is characterized in that: the 4th reaction tank being positioned at tail end in described secondary reaction pool unit is communicated with via the 4th transferpump is corresponding with described post-precipitate pond.
10. Zinc Sulphate Monohydrate production wastewater treatment system as claimed in claim 2, is characterized in that: described post-precipitate pond is communicated with via the 5th transferpump is corresponding with described secondary pressure filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520515496.6U CN204897573U (en) | 2015-07-16 | 2015-07-16 | Sulfuric acid monohydrate zinc waste water processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520515496.6U CN204897573U (en) | 2015-07-16 | 2015-07-16 | Sulfuric acid monohydrate zinc waste water processing system |
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| Publication Number | Publication Date |
|---|---|
| CN204897573U true CN204897573U (en) | 2015-12-23 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520515496.6U Active CN204897573U (en) | 2015-07-16 | 2015-07-16 | Sulfuric acid monohydrate zinc waste water processing system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110803804A (en) * | 2019-11-27 | 2020-02-18 | 衡阳旭光锌锗科技有限公司 | Wastewater treatment system for zinc sulfate production |
-
2015
- 2015-07-16 CN CN201520515496.6U patent/CN204897573U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110803804A (en) * | 2019-11-27 | 2020-02-18 | 衡阳旭光锌锗科技有限公司 | Wastewater treatment system for zinc sulfate production |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Sulfuric acid monohydrate zinc waste water processing system Effective date of registration: 20191210 Granted publication date: 20151223 Pledgee: Bank of China Limited by Share Ltd. Pingxiang branch Pledgor: JIANGXI BAOHAI WEIYUAN REGENERATION SCIENCE & TECHNOLOGY Co.,Ltd. Registration number: Y2019360000035 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20201224 Granted publication date: 20151223 Pledgee: Bank of China Limited by Share Ltd. Pingxiang branch Pledgor: JIANGXI BAOHAI WEIYUAN REGENERATION SCIENCE & TECHNOLOGY Co.,Ltd. Registration number: Y2019360000035 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Zinc sulfate monohydrate production wastewater treatment system Effective date of registration: 20211203 Granted publication date: 20151223 Pledgee: Bank of China Limited by Share Ltd. Pingxiang branch Pledgor: JIANGXI BAOHAI WEIYUAN REGENERATION SCIENCE & TECHNOLOGY Co.,Ltd. Registration number: Y2021980014002 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Granted publication date: 20151223 Pledgee: Bank of China Limited by Share Ltd. Pingxiang branch Pledgor: JIANGXI BAOHAI WEIYUAN REGENERATION SCIENCE & TECHNOLOGY Co.,Ltd. Registration number: Y2021980014002 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |