CN106552599A - A kind of active mineral drier - Google Patents
A kind of active mineral drier Download PDFInfo
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- CN106552599A CN106552599A CN201510640559.5A CN201510640559A CN106552599A CN 106552599 A CN106552599 A CN 106552599A CN 201510640559 A CN201510640559 A CN 201510640559A CN 106552599 A CN106552599 A CN 106552599A
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- drier
- active mineral
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- mineral drier
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Abstract
The invention discloses a kind of active mineral drier, it is characterised in that the dispensing of active mineral drier is made up of following component by weight：15～45 parts of attapulgite clay, carclazyte 10-36 parts, calcium chloride 30～60% and high hydroscopic resin 0.1～5%；The production method of described active mineral drier：The dispensing input mixer of active mineral drier is mixed, is packed after stirring as active mineral drier；The dispensing of the active mineral drier is made up of following component by weight：60～85 parts of tablet after drying and attapulgite clay powder 15～45%；The present invention is jointly milled, is granulated and is roasted to spherical concave convex rod drier with the dolomite Concave-convex clay rod after acidification using Concave-convex clay rod powder, substantially increases the adsorption capacity and granule strength of drying agent for ball-shaped container.
Description
Technical field
The present invention relates to drier technical field, more particularly to a kind of active mineral drier.
Background technology
Ore deposit living can be widely used for not adopting oil sealing to deposit, in the product that gas phase is sealed up for safekeeping, such as the product for civilian use and war products such as precision instrument, electronic product, medicines and health protection product, packaging for foodstuff, clothes, shoes and hats, and for Container Transport.
The content of the invention
It is an object of the invention to provide a kind of active mineral drier, environmental protection, safety, can regenerate use, hygroscopicity is high, go peculiar smell ability strong, nonpoisonous and tasteless, contactless property corrosion, non-environmental-pollution..
To achieve these goals, the present invention is adopted the following technical scheme that：
A kind of active mineral drier, it is characterised in that the dispensing of active mineral drier is made up of following component by weight：15～45 parts of attapulgite clay, carclazyte 10-36 parts, calcium chloride 30～60% and high hydroscopic resin 0.1～5%；
The production method of described active mineral drier：The dispensing input mixer of active mineral drier is mixed, is packed after stirring as active mineral drier；The dispensing of the active mineral drier is made up of following component by weight：60～85 parts of tablet after drying and attapulgite clay powder 15～45%；
The production method of described active mineral drier：
1) add stirring mixer to be mixed the dispensing of spherical concave convex rod drier, be input in grinding machine after being well mixed and wear into powder, grain fineness≤0.04 millimeter of powder；
2) powder is input in comminutor and is granulated, the particle after granulation is spherical in shape, spherical particle diameters are controlled at 0.5～5.0 millimeter；
3) spheric granules is input in roaster carries out roasting, sintering temperature is controlled at 250～320 DEG C, roasting time was controlled at 60～180 minutes, spheric granules is sieved after roasting cooling, the crushed particles produced in roasting process and powder are screened out, it is spherical concave convex rod drier after screening, water content≤2% of spherical concave convex rod drier.
The production method of the tablet after the drying：
1）Dolomite Concave-convex clay rod is crushed, grain fineness≤0.50 millimeter after crushing；
2）The preparation of dilute sulfuric acid is made up of following component by weight percentage：The sulfuric acid 1～20% and water 80～99% of 98 ﹪ of concentration；
3）The dispensing of acidification is made up of following component by weight percentage：Dolomite Concave-convex clay rod 55～75% and dilute sulfuric acid 25～45%；
4）Dilute sulfuric acid is slowly added to acidification is carried out in dolomite Concave-convex clay rod, after the dolomite Concave-convex clay rod after acidified process is stacked 24～72 hours, is extruded in input twin rollers as tablet, thickness≤3 millimeter of tablet；
Tablet is transported to cement court to be dried, water content≤15% in the tablet after drying；The high viscous Concave-convex clay rod powder is referred to and takes 28.0g Concave-convex clay rod powder samples, in adding the suspension cup of homogenizer, add 372g water, suspension cup is placed on homogenizer, stir 20 minutes under 11000 revs/min of rotating speed, again by the beaker that high-speed stirred sample suspension pours 250ml into, carry out testing the viscosity of its suspension using NDJ-1 types rotation viscometer, the Concave-convex clay rod powder of tested viscosity value >=2200 mPas is high viscous Concave-convex clay rod powder.
Beneficial effects of the present invention：
The present invention is jointly milled, is granulated and is roasted to spherical concave convex rod drier with the dolomite Concave-convex clay rod after acidification using Concave-convex clay rod powder, the adsorption capacity and granule strength of drying agent for ball-shaped container are substantially increased, concave convex rod drier can absorb the aqueous water equivalent to own wt >=65%.
Specific embodiment
Below, the present invention will be further described in conjunction with the embodiments.
A kind of active mineral drier, it is characterised in that the dispensing of active mineral drier is made up of following component by weight：15～45 parts of attapulgite clay, carclazyte 10-36 parts, calcium chloride 30～60% and high hydroscopic resin 0.1～5%；The production method of described active mineral drier：The dispensing input mixer of active mineral drier is mixed, is packed after stirring as active mineral drier；The dispensing of the active mineral drier is made up of following component by weight：60～85 parts of tablet after drying and attapulgite clay powder 15～45%.
The production method of described active mineral drier：
1) add stirring mixer to be mixed the dispensing of spherical concave convex rod drier, be input in grinding machine after being well mixed and wear into powder, grain fineness≤0.04 millimeter of powder；
2) powder is input in comminutor and is granulated, the particle after granulation is spherical in shape, spherical particle diameters are controlled at 0.5～5.0 millimeter；
3) spheric granules is input in roaster carries out roasting, sintering temperature is controlled at 250～320 DEG C, roasting time was controlled at 60～180 minutes, spheric granules is sieved after roasting cooling, the crushed particles produced in roasting process and powder are screened out, it is spherical concave convex rod drier after screening, water content≤2% of spherical concave convex rod drier.
The production method of the tablet after the drying：
2）Dolomite Concave-convex clay rod is crushed, grain fineness≤0.50 millimeter after crushing；
2）The preparation of dilute sulfuric acid is made up of following component by weight percentage：The sulfuric acid 1～20% and water 80～99% of 98 ﹪ of concentration；
3）The dispensing of acidification is made up of following component by weight percentage：Dolomite Concave-convex clay rod 55～75% and dilute sulfuric acid 25～45%；
4）Dilute sulfuric acid is slowly added to acidification is carried out in dolomite Concave-convex clay rod, after the dolomite Concave-convex clay rod after acidified process is stacked 24～72 hours, is extruded in input twin rollers as tablet, thickness≤3 millimeter of tablet.
Tablet is transported to cement court to be dried, water content≤15% in the tablet after drying；The high viscous Concave-convex clay rod powder is referred to and takes 28.0g Concave-convex clay rod powder samples, in adding the suspension cup of homogenizer, add 372g water, suspension cup is placed on homogenizer, stir 20 minutes under 11000 revs/min of rotating speed, again by the beaker that high-speed stirred sample suspension pours 250ml into, carry out testing the viscosity of its suspension using NDJ-1 types rotation viscometer, the Concave-convex clay rod powder of tested viscosity value >=2200 mPas is high viscous Concave-convex clay rod powder.
Above example only not limits technical scheme described in the invention to illustrate the present invention；Therefore, although this specification with reference to each above-mentioned embodiment to present invention has been detailed description, it will be understood by those within the art that, still the present invention can be modified or equivalent；And all are without departing from technical scheme and its improvement of the spirit and scope of the present invention, all should cover in scope of the presently claimed invention.
Claims (1)
1. a kind of active mineral drier, it is characterised in that the dispensing of active mineral drier is made up of following component by weight
：15～45 parts of attapulgite clay, carclazyte 10-36 parts, calcium chloride 30～60% and high hydroscopic resin 0.1～5%；
The production method of described active mineral drier：The dispensing input mixer of active mineral drier is mixed, is packed after stirring as active mineral drier；The dispensing of the active mineral drier is made up of following component by weight
：60～85 parts of tablet after drying and attapulgite clay powder 15～45%；
The production method of described active mineral drier：
1) add stirring mixer to be mixed the dispensing of spherical concave convex rod drier, be input in grinding machine after being well mixed and wear into powder, grain fineness≤0.04 millimeter of powder；
2) powder is input in comminutor and is granulated, the particle after granulation is spherical in shape, spherical particle diameters are controlled at 0.5～5.0 millimeter；
3) spheric granules is input in roaster carries out roasting, and sintering temperature control exists
250～320 DEG C, at 60～180 minutes, spheric granules was sieved after roasting cooling, and the crushed particles produced in roasting process and powder are screened out for roasting time control, it is spherical concave convex rod drier after screening, water content≤2% of spherical concave convex rod drier.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510640559.5A CN106552599A (en) | 2015-09-30 | 2015-09-30 | A kind of active mineral drier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510640559.5A CN106552599A (en) | 2015-09-30 | 2015-09-30 | A kind of active mineral drier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106552599A true CN106552599A (en) | 2017-04-05 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510640559.5A Pending CN106552599A (en) | 2015-09-30 | 2015-09-30 | A kind of active mineral drier |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108464430A (en) * | 2018-04-09 | 2018-08-31 | 袁国森 | A kind of food desiccant and preparation method thereof |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1422687A (en) * | 2001-12-06 | 2003-06-11 | 吴才来 | Mineral drying agent |
| CN1559665A (en) * | 2004-03-09 | 2005-01-05 | 杜建中 | Concave-convex rod clay composite drying agent |
| JP4475048B2 (en) * | 2004-07-30 | 2010-06-09 | 凸版印刷株式会社 | Variable shape drying member |
| CN102327729A (en) * | 2011-07-26 | 2012-01-25 | 许盛英 | Drying agent for bar-shaped container |
| CN102327734A (en) * | 2011-07-21 | 2012-01-25 | 许盛英 | Drying agent for ball-shaped container |
| CN102350188A (en) * | 2011-07-21 | 2012-02-15 | 许盛英 | Powdery drying agent for containers |
-
2015
- 2015-09-30 CN CN201510640559.5A patent/CN106552599A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1422687A (en) * | 2001-12-06 | 2003-06-11 | 吴才来 | Mineral drying agent |
| CN1559665A (en) * | 2004-03-09 | 2005-01-05 | 杜建中 | Concave-convex rod clay composite drying agent |
| JP4475048B2 (en) * | 2004-07-30 | 2010-06-09 | 凸版印刷株式会社 | Variable shape drying member |
| CN102327734A (en) * | 2011-07-21 | 2012-01-25 | 许盛英 | Drying agent for ball-shaped container |
| CN102350188A (en) * | 2011-07-21 | 2012-02-15 | 许盛英 | Powdery drying agent for containers |
| CN102327729A (en) * | 2011-07-26 | 2012-01-25 | 许盛英 | Drying agent for bar-shaped container |
Non-Patent Citations (1)
| Title |
|---|
| 谭世语等: "《化工工艺学》", 31 January 2015, 重庆大学出版社出版发行 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108464430A (en) * | 2018-04-09 | 2018-08-31 | 袁国森 | A kind of food desiccant and preparation method thereof |
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Application publication date: 20170405 |