CN107837784A - A kind of packaging bag printing ink preprocess method - Google Patents
A kind of packaging bag printing ink preprocess method Download PDFInfo
- Publication number
- CN107837784A CN107837784A CN201711068692.3A CN201711068692A CN107837784A CN 107837784 A CN107837784 A CN 107837784A CN 201711068692 A CN201711068692 A CN 201711068692A CN 107837784 A CN107837784 A CN 107837784A
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- CN
- China
- Prior art keywords
- flyash
- packaging bag
- printing ink
- raw material
- preprocess method
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention discloses a kind of packaging bag printing ink preprocess method, specifically comprise the following steps：S1：Raw material prepares, S2：Flyash pre-processes, S3：Flyash is ground, S4：Flyash sieves, S5：Raw material mixes, S6：The mixed material obtained in step S5 is added into pending ink, is stirred in addition, the reaction time between 1h 1.5h, stands 30min, finally again extracted lower sediment thing out, percent of decolourization is up to more than 90%, CODCrClearance more than 70%.Flyash is used as raw material, raw material sources are wide, reduce raw material production cost, by the way that the flyash of bulk is crushed, and it will be ground by grinder, make flyash in powdered, be easy to flyash and the follow-up mixing of PDDA, the material after being sufficiently mixed, purified treatment can be carried out to the waste water containing ink, strict control reaction time and reaction temperature, operating efficiency is high, ensures clean-up effect.
Description
Technical field
The invention belongs to ink preconditioning technique field, more specifically, more particularly to a kind of packaging bag printing ink
Preprocess method.
Background technology
With the continuous progress of technology, the application of packaging bag is also more and more extensive, and packaging bag refers to be used to pack various use
The sack of product, make goods convenience in transport in the process of circulation is produced, easily storage.It is widely used in daily life and industrial production
In.Real figure shows there is the polybag after 80% use, the processing of rubbish heap field area is finally transported to as conventional rubbish, only
The plastics for having 7 percent are recovered recycling.With the fast development of China's economy, the purchasing power of domestic resident it is horizontal and
Consumption wish also progressively strengthens, and consumption idea will tend to further improve the quality of living.Beverage, drinks, edible oil and flavouring
The market demand Deng food liquid also will steady-state growth with the economic development and improvement of people's living standards.Packaging itself
Commodity is also more and more significant, and it turns into a kind of specialities for no longer depending on commodity production, a kind of all commodity all from
Product do not open, wide variety of.
Packaging bag printing ink has very important status in packaging bag production, and printing ink wastewater is always at waste water
One of difficult point of reason, now lacks a kind of packaging bag printing ink preprocess method, and traditional packaging bag printing ink is located in advance
Reason method cost is high, and treatment effect is difficult to ensure that, it is impossible to meets ecological requirements, it is necessary to further optimization and perfect.
The content of the invention
The invention aims to solve shortcoming present in prior art, and a kind of packaging bag printing proposed is oily
Black preprocess method.
To achieve the above object, the present invention provides following technical scheme：A kind of packaging bag printing ink preprocess method,
Specifically comprise the following steps：
S1：Raw material prepares, and commercially buys flyash and PDDA, standby；
S2：Flyash pre-process, the flyash purchased in step S1 is added in pulverizer, using pulverizer by bulk powder
Coal ash is ground into graininess, and collects standby；
S3：Flyash is ground, and the step S2 flyash obtained is added in grinder, using grinder by granular fine coal
Ash is ground into powder, and collects standby；
S4：Flyash is sieved, and the powdered flyash of the acquisition in step S3 is sieved, and using 120 mesh sieves, will be obtained after sieving
The flyash collection obtained is standby, and will continue to grind in the grinder in unsifted powder transferring to step S3, is easy to fully
Utilize fly ash；
S5：Raw material mixes, the poly dimethyl diene that will be purchased in the flyash powder after being sieved in step S4 and step S1
Propyl ammonium chloride is added in mixer simultaneously to be stirred, mixed proportion 1000:23, after mixing is completed, collect standby；
S6：The mixed material obtained in step S5 is added into pending ink, is stirred in addition, the reaction time is in 1h-
Between 1.5h；
S7：30min is stood, is finally again extracted lower sediment thing out, percent of decolourization is up to more than 90%, CODCrClearance exceed
70%。
Preferably, the PDDA commercially purchased in the step S1 is in powdered.
Preferably, the rotating speed of pulverizer is 1200r/min in the step S2, grinding time control 0.2h-0.25h it
Between, temperature is crushed between 10-50 degrees Celsius.
Preferably, the rotating speed of grinder is 1000r/min in the step S3, milling time control 0.2h-0.3h it
Between, grinding temperature is between 10-60 degrees Celsius.
Preferably, the rotating speed of mixer is 1100r/min in the step S2, mixing time control 0.3h-0.5h it
Between, whipping temp is no more than 60 degrees Celsius.
Preferably, the reaction temperature in the step S6 is 35 degrees Celsius, easily right using the heating means of heating water bath
Water temperature is controlled.
The technique effect and advantage of the present invention：A kind of packaging bag printing ink preprocess method of the present invention, using fine coal
Ash is raw material, and raw material sources are wide, reduces raw material production cost, by the way that the flyash of bulk is crushed, and will be ground by grinder
Mill, make flyash in powdered, be easy to flyash and the follow-up mixing of PDDA, be sufficiently mixed
Material afterwards, for the flyash inorganic agent of improvement, flyash has porous adsorption structure, poly dimethyl allyl in itself
Ammonium chloride auxiliary sedimentation, purified treatment can be carried out to the waste water containing ink, percent of decolourization is up to more than 90%, CODCrRemoval
For rate more than 70%, strict to control reaction time and reaction temperature, operating efficiency is high, ensures clean-up effect.
Embodiment
In order to make the purpose , technical scheme and advantage of the present invention be clearer, below in conjunction with specific embodiment, to this
Invention is further elaborated.It should be appreciated that the specific embodiments described herein are merely illustrative of the present invention, not
For limiting the present invention.Based on the embodiment in the present invention, those of ordinary skill in the art are not before creative work is made
The every other embodiment obtained is put, belongs to the scope of protection of the invention.
A kind of packaging bag printing ink preprocess method provided by the invention, specifically comprises the following steps：
S1：Raw material prepares, and commercially buys flyash and PDDA, standby；
S2：Flyash pre-process, the flyash purchased in step S1 is added in pulverizer, using pulverizer by bulk powder
Coal ash is ground into graininess, and collects standby；
S3：Flyash is ground, and the step S2 flyash obtained is added in grinder, using grinder by granular fine coal
Ash is ground into powder, and collects standby；
S4：Flyash is sieved, and the powdered flyash of the acquisition in step S3 is sieved, and using 120 mesh sieves, will be obtained after sieving
The flyash collection obtained is standby, and will continue to grind in the grinder in unsifted powder transferring to step S3, is easy to fully
Utilize fly ash；
S5：Raw material mixes, the poly dimethyl diene that will be purchased in the flyash powder after being sieved in step S4 and step S1
Propyl ammonium chloride is added in mixer simultaneously to be stirred, mixed proportion 1000:23, after mixing is completed, collect standby；
S6：The mixed material obtained in step S5 is added into pending ink, is stirred in addition, the reaction time is in 1h-
Between 1.5h；
S7：30min is stood, is finally again extracted lower sediment thing out, percent of decolourization is up to more than 90%, CODCrClearance exceed
70%。
The PDDA commercially purchased in the step S1 is in powdered, the step S2
The rotating speed of middle pulverizer is 1200r/min, and grinding time is controlled between 0.2h-0.25h, crushes temperature at 10-50 degrees Celsius
Between, the rotating speed of grinder is 1000r/min in the step S3, and milling time is controlled between 0.2h-0.3h, grinding temperature
Between 10-60 degrees Celsius, the rotating speed of mixer is 1100r/min in the step S2, and mixing time is controlled in 0.3h-0.5h
Between, for whipping temp no more than 60 degrees Celsius, the reaction temperature in the step S6 is 35 degrees Celsius, using adding for heating water bath
Hot method, is easily controlled to water temperature.
In summary：A kind of packaging bag printing ink preprocess method of the present invention, uses flyash as raw material, and raw material comes
Source is wide, reduces raw material production cost, by the way that the flyash of bulk is crushed, and will be ground by grinder, it is in powder to make flyash
Last shape, it is easy to flyash and the follow-up mixing of PDDA, the material after being sufficiently mixed, to change
Good flyash inorganic agent, flyash have porous adsorption structure in itself, and PDDA auxiliary settles,
Purified treatment can be carried out to the waste water containing ink, percent of decolourization is up to more than 90%, CODCrClearance more than 70%, strict control
Reaction time processed and reaction temperature, operating efficiency is high, ensures clean-up effect.
In the present invention, unless otherwise clearly defined and limited, term " installation ", " connected ", " connection ", " fixation " etc.
Term should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected, or be integrally connected；It can be machine
Tool connects or electrical connection；Can be joined directly together, can also be indirectly connected by intermediary, can be two members
Connection inside part.For the ordinary skill in the art, above-mentioned term can be understood in this hair as the case may be
Concrete meaning in bright.
Finally it should be noted that：The preferred embodiments of the present invention are the foregoing is only, are not intended to limit the invention,
Although the present invention is described in detail with reference to the foregoing embodiments, for those skilled in the art, it still may be used
To be modified to the technical scheme described in foregoing embodiments, or equivalent substitution is carried out to which part technical characteristic,
Within the spirit and principles of the invention, any modification, equivalent substitution and improvements made etc., it should be included in the present invention's
Within protection domain.
Claims (6)
- A kind of 1. packaging bag printing ink preprocess method, it is characterised in that：Specifically comprise the following steps：S1：Raw material prepares, and commercially buys flyash and PDDA, standby；S2：Flyash pre-process, the flyash purchased in step S1 is added in pulverizer, using pulverizer by bulk powder Coal ash is ground into graininess, and collects standby；S3：Flyash is ground, and the step S2 flyash obtained is added in grinder, using grinder by granular fine coal Ash is ground into powder, and collects standby；S4：Flyash is sieved, and the powdered flyash of the acquisition in step S3 is sieved, and using 120 mesh sieves, will be obtained after sieving The flyash collection obtained is standby, and will continue to grind in the grinder in unsifted powder transferring to step S3, is easy to fully Utilize fly ash；S5：Raw material mixes, the poly dimethyl diene that will be purchased in the flyash powder after being sieved in step S4 and step S1 Propyl ammonium chloride is added in mixer simultaneously to be stirred, mixed proportion 1000:23, after mixing is completed, collect standby；S6：The mixed material obtained in step S5 is added into pending ink, is stirred in addition, the reaction time is in 1h- Between 1.5h；S7：30min is stood, is finally again extracted lower sediment thing out, percent of decolourization is up to more than 90%, CODCrClearance exceed 70%。
- A kind of 2. packaging bag printing ink preprocess method according to claim 1, it is characterised in that：The step S1 In the PDDA commercially purchased in powdered.
- A kind of 3. packaging bag printing ink preprocess method according to claim 1, it is characterised in that：The step S2 The rotating speed of middle pulverizer is 1200r/min, and grinding time is controlled between 0.2h-0.25h, crushes temperature at 10-50 degrees Celsius Between.
- A kind of 4. packaging bag printing ink preprocess method according to claim 1, it is characterised in that：The step S3 The rotating speed of middle grinder is 1000r/min, and milling time is controlled between 0.2h-0.3h, grinding temperature 10-60 degrees Celsius it Between.
- A kind of 5. packaging bag printing ink preprocess method according to claim 1, it is characterised in that：The step S2 The rotating speed of middle mixer is 1100r/min, and mixing time is controlled between 0.3h-0.5h, and whipping temp is no more than 60 degrees Celsius.
- A kind of 6. packaging bag printing ink preprocess method according to claim 1, it is characterised in that：The step S6 In reaction temperature be 35 degrees Celsius, using the heating means of heating water bath, easily water temperature is controlled.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711068692.3A CN107837784A (en) | 2017-11-03 | 2017-11-03 | A kind of packaging bag printing ink preprocess method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711068692.3A CN107837784A (en) | 2017-11-03 | 2017-11-03 | A kind of packaging bag printing ink preprocess method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107837784A true CN107837784A (en) | 2018-03-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711068692.3A Pending CN107837784A (en) | 2017-11-03 | 2017-11-03 | A kind of packaging bag printing ink preprocess method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113754115A (en) * | 2021-09-09 | 2021-12-07 | 深圳瑞赛环保科技有限公司 | Catalytic filler for PCB (printed Circuit Board) ink wastewater pretreatment, preparation method and treatment method and equipment |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104826578A (en) * | 2015-05-29 | 2015-08-12 | 浙江海洋学院 | Fly ash modified adsorbent and preparing method thereof and method of treating oily sewage |
| CN107188286A (en) * | 2017-05-27 | 2017-09-22 | 郑州沃煌环保技术有限公司 | Multi-functional sewage handles coagulant |
-
2017
- 2017-11-03 CN CN201711068692.3A patent/CN107837784A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104826578A (en) * | 2015-05-29 | 2015-08-12 | 浙江海洋学院 | Fly ash modified adsorbent and preparing method thereof and method of treating oily sewage |
| CN107188286A (en) * | 2017-05-27 | 2017-09-22 | 郑州沃煌环保技术有限公司 | Multi-functional sewage handles coagulant |
Non-Patent Citations (2)
| Title |
|---|
| 岳钦艳等: "PDMDAAC改性粉煤灰的制备及其脱色效果研究", 《中国给水排水》 * |
| 肖杰等: "PDMDAAC改性粉煤灰预处理油墨废水的研究", 《四川环境》 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113754115A (en) * | 2021-09-09 | 2021-12-07 | 深圳瑞赛环保科技有限公司 | Catalytic filler for PCB (printed Circuit Board) ink wastewater pretreatment, preparation method and treatment method and equipment |
| CN113754115B (en) * | 2021-09-09 | 2024-01-23 | 深圳瑞赛环保科技有限公司 | PCB (printed circuit board) ink wastewater pretreatment catalytic filler, preparation method and treatment method and equipment |
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Application publication date: 20180327 |
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