CN106219789A - A kind of irrigation oozes HDPE tubing with micro- - Google Patents

A kind of irrigation oozes HDPE tubing with micro- Download PDF

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Publication number
CN106219789A
CN106219789A CN201610762973.8A CN201610762973A CN106219789A CN 106219789 A CN106219789 A CN 106219789A CN 201610762973 A CN201610762973 A CN 201610762973A CN 106219789 A CN106219789 A CN 106219789A
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CN
China
Prior art keywords
parts
irrigation
micro
oxide
oozes
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.)
Withdrawn
Application number
CN201610762973.8A
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Chinese (zh)
Inventor
卢震宇
朱建华
汪进南
史青林
黄剑锋
余为华
胡亮亮
傅蒙
汪燕飞
张成洋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ANHUI YONGGAO PLASTIC INDUSTRY DEVELOPMENT Co Ltd
Original Assignee
ANHUI YONGGAO PLASTIC INDUSTRY DEVELOPMENT Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by ANHUI YONGGAO PLASTIC INDUSTRY DEVELOPMENT Co Ltd filed Critical ANHUI YONGGAO PLASTIC INDUSTRY DEVELOPMENT Co Ltd
Priority to CN201610762973.8A priority Critical patent/CN106219789A/en
Publication of CN106219789A publication Critical patent/CN106219789A/en
Withdrawn legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/30—Particle separators, e.g. dust precipitators, using loose filtering material
    • 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
    • B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/041—Oxides or hydroxides
    • 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
    • B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/048—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium containing phosphorus, e.g. phosphates, apatites, hydroxyapatites
    • 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
    • B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • 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
    • 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
    • B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • 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
    • C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
    • 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
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00—General aspects of water treatment
    • C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

A kind of irrigation oozes HDPE tubing with micro-, and sponge includes spongiosum, and spongiosum includes some spongy bodies, is provided with filter course between some spongy bodies；Spongy body is provided with snakelike filter opening, and filter opening inwall is provided with adsorption layer；Filter opening inwall is provided with some holes, is provided with activated carbon in described hole.By the sponge of the present invention, can effectively cross the impurity in air filtering or liquid.Prepare adsorbing material by cordierite, mullite, silochrom, montmorillonite, activated alumina, calcium sulfate, dimethicone, sodium alginate, monkey grass, there is good absorption property.Sponge itself has good strainability, adds the setting of snakelike filter opening, it is ensured that needs filtered air or liquid are had sufficient filtration time.

Description

A kind of irrigation oozes HDPE tubing with micro-
Technical field
The present invention relates to irrigate tubing field, especially a kind of irrigation and ooze HDPE tubing with micro-.
Background technology
The water pipe of existing irrigation is typically all and seals, and is connected to shower nozzle if needing irrigation to need individually, now Market is to irrigate in the urgent need to one to ooze HDPE tubing with micro-.
Summary of the invention
The technical problem that present invention mainly solves is to provide a kind of irrigation to ooze HDPE tubing with micro-.
The present invention solves that the technical scheme that above-mentioned technical problem uses is:
A kind of irrigation oozes HDPE tubing with micro-, includes tube body, is provided with logical between outer wall and the inwall of described tube body Hole, is filled with sponge in described through hole；Described sponge includes spongiosum, and described spongiosum includes some spongy bodies, It is provided with filter course between described some spongy bodies；Described spongy body is provided with snakelike filter opening, and described filter opening inwall is provided with absorption Layer；Described filter opening inwall is provided with some holes, is provided with activated carbon in described hole；
Described filter course include stack successively HEPA filter course, Alveolate activated carbon drainage screen, cellular nano silver Sponge drainage screen；Described HEPA filter course is stacked by the HEPA filter screen of the 35-45 layer stacked successively and constitutes；
Described adsorption layer component by weight is: cordierite 13-15 part, mullite 9-11 part, silochrom 6-8 part, illiteracy De-stone 4-7 part, activated alumina 8-10 part, calcium sulfate 3-5 part, dimethicone 2-3 part, sodium alginate 3-4 part, monkey grass 3-5 part, carbamide 2-3 part, silica gel 10-20 part, Kaolin 5-15 part, zeolite 6-10 part, aluminium oxide 1-5 part, aluminium glue 2-5 part, oxygen Change calcium 1-3 part, zinc oxide 1-2 part, sesbania powder 1-3 part.
Further, described adsorption layer component by weight is: cordierite 14 parts, mullite 10 parts, silochrom 7 parts, Montmorillonite 5 parts, activated alumina 9 parts, 4 parts of calcium sulfate, dimethicone 3 parts, sodium alginate 3 parts, monkey grass 4 parts, carbamide 3 Part, 15 parts of silica gel, Kaolin 10 parts, 8 parts of zeolite, aluminium oxide 3 parts, aluminium glue 4 parts, calcium oxide 2 parts, zinc oxide 1 part, sesbania powder 2 Part.
Further, the preparation method of described adsorption layer is:
A. take aluminium glue, calcium oxide, zinc oxide, sesbania powder, uniformly after mixing, through kneading, molding, pelletizing, primary drying, One time roasting, dipping, redrying, after baking obtain dehydrant；
B., silica gel is crossed 150 mesh sieves, and Kaolin crosses 200 mesh sieves, and zeolite crosses 80 mesh sieves, and aluminium oxide crosses 325 mesh sieves, then depends on Secondary by the mixing of the silica gel sieved, Kaolin, zeolite and aluminium oxide, obtain adsorbent first product；
C. cordierite, mullite, silochrom, montmorillonite, activated alumina, calcium sulfate, dimethicone, alginic acid are taken Grind after the mixing of sodium, monkey grass, be then dried process, obtain adsorbent mixtures；
D. distillation is added with the adsorbent mixtures obtained in step c after being mixed by the adsorbent first product obtained in step b Water, puts in blender with rotating speed for the continuously stirred 30-45min of 1800r/min, obtains adsorbent, the absorption that then will obtain Agent adds the dehydrant in step a, puts into and carries out drying operation in dehydrator, obtains adsorbing material, and adsorbing material i.e. prepares to be inhaled Attached layer.
Further, some filter course being distributed on described adsorption layer, described filter course component by weight includes: powder Broken coconut husk 20-25 part, zirconium oxide 5-8 part, micropowder silica gel 3-5 part.
Further, the preparation method of described filter course is: will pulverize coconut husk hot wash, and use the most at normal temperatures 50-60% phosphoric acid solution soaks 1-2 hour；Filter, take filtering residue carbonization 1.5-2 hour in the retort of 550-600 DEG C, take Go out；Mix homogeneously with zirconium oxide, micropowder silica gel when temperature is down to room temperature, add 60% sodium hydroxide and stir 1-1.5 hour, Then taking-up is filtered；Clean 3-4 time with distilled water, drying.
The invention have the benefit that
By the sponge of the present invention, can effectively cross the impurity in air filtering or liquid.
By cordierite, mullite, silochrom, montmorillonite, activated alumina, calcium sulfate, dimethicone, alginic acid Sodium, monkey grass prepare adsorbing material, have good absorption property.
Sponge itself has good strainability, adds the setting of snakelike filter opening, it is ensured that to the sky needing filtration Gas or liquid have sufficient filtration time.
Accompanying drawing explanation
Fig. 1 is the structural representation of sponge in a kind of detailed description of the invention of the present invention.
In figure: 1 is spongy body, 2 is filter course, and 3 is snakelike filter opening.
Detailed description of the invention
The present invention is further elaborated below in conjunction with the accompanying drawings.
A kind of irrigation oozes HDPE tubing with micro-, includes tube body, is provided with logical between outer wall and the inwall of described tube body Hole, is filled with sponge in described through hole；Sponge includes spongiosum, and described spongiosum includes some spongy bodies, described It is provided with filter course between some spongy bodies；Described spongy body is provided with snakelike filter opening, and described filter opening inwall is provided with adsorption layer；
Described filter opening inwall is provided with some holes, is provided with activated carbon in described hole；
Described filter course include stack successively HEPA filter course, Alveolate activated carbon drainage screen, cellular nano silver Sponge drainage screen；Described HEPA filter course is stacked by the HEPA filter screen of the 35-45 layer stacked successively and constitutes；
Described adsorption layer component by weight is: cordierite 13-15 part, mullite 9-11 part, silochrom 6-8 part, illiteracy De-stone 4-7 part, activated alumina 8-10 part, calcium sulfate 3-5 part, dimethicone 2-3 part, sodium alginate 3-4 part, monkey grass 3-5 part, carbamide 2-3 part, silica gel 10-20 part, Kaolin 5-15 part, zeolite 6-10 part, aluminium oxide 1-5 part, aluminium glue 2-5 part, oxygen Change calcium 1-3 part, zinc oxide 1-2 part, sesbania powder 1-3 part.
Further, described adsorption layer component by weight is: cordierite 14 parts, mullite 10 parts, silochrom 7 parts, Montmorillonite 5 parts, activated alumina 9 parts, 4 parts of calcium sulfate, dimethicone 3 parts, sodium alginate 3 parts, monkey grass 4 parts, carbamide 3 Part, 15 parts of silica gel, Kaolin 10 parts, 8 parts of zeolite, aluminium oxide 3 parts, aluminium glue 4 parts, calcium oxide 2 parts, zinc oxide 1 part, sesbania powder 2 Part.
Further, the preparation method of described adsorption layer is:
A. take aluminium glue, calcium oxide, zinc oxide, sesbania powder, uniformly after mixing, through kneading, molding, pelletizing, primary drying, One time roasting, dipping, redrying, after baking obtain dehydrant；
B., silica gel is crossed 150 mesh sieves, and Kaolin crosses 200 mesh sieves, and zeolite crosses 80 mesh sieves, and aluminium oxide crosses 325 mesh sieves, then depends on Secondary by the mixing of the silica gel sieved, Kaolin, zeolite and aluminium oxide, obtain adsorbent first product；
C. cordierite, mullite, silochrom, montmorillonite, activated alumina, calcium sulfate, dimethicone, alginic acid are taken Grind after the mixing of sodium, monkey grass, be then dried process, obtain adsorbent mixtures；
D. distillation is added with the adsorbent mixtures obtained in step c after being mixed by the adsorbent first product obtained in step b Water, puts in blender with rotating speed for the continuously stirred 30-45min of 1800r/min, obtains adsorbent, the absorption that then will obtain Agent adds the dehydrant in step a, puts into and carries out drying operation in dehydrator, obtains adsorbing material, and adsorbing material i.e. prepares to be inhaled Attached layer.
Some filter course is distributed on adsorption layer, and described filter course component by weight includes: pulverize coconut husk 20-25 Part, zirconium oxide 5-8 part, micropowder silica gel 3-5 part；The preparation method of filter course is: will pulverize coconut husk hot wash, then often Temperature is lower soaks 1-2 hour with 50-60% phosphoric acid solution；Filter, take filtering residue carbonization 1.5-2 in the retort of 550-600 DEG C little Time, take out；Mix homogeneously with zirconium oxide, micropowder silica gel when temperature is down to room temperature, add 60% sodium hydroxide stirring 1-1.5 Hour, then filter taking-up；Clean 3-4 time with distilled water, drying.
By the sponge of the present invention, can effectively cross the impurity in air filtering or liquid；By cordierite, mullite, thick Hole silica gel, montmorillonite, activated alumina, calcium sulfate, dimethicone, sodium alginate, monkey grass prepare adsorbing material, have Good absorption property；Sponge itself has good strainability, adds the setting of snakelike filter opening, it is ensured that to needs Air or the liquid of filter have sufficient filtration time.

Claims (5)

1. an irrigation oozes HDPE tubing with micro-, it is characterised in that: include tube body, the outer wall of described tube body and inwall it Between be provided with through hole, be filled with sponge in described through hole；Described sponge includes spongiosum, and described spongiosum includes some Spongy body, is provided with filter course between described some spongy bodies；Described spongy body is provided with snakelike filter opening, and described filter opening inwall sets There is adsorption layer；
Described filter opening inwall is provided with some holes, is provided with activated carbon in described hole；
Described filter course include stack successively HEPA filter course, Alveolate activated carbon drainage screen, cellular nano silver sponge Drainage screen；Described HEPA filter course is stacked by the HEPA filter screen of the 35-45 layer stacked successively and constitutes；
Described adsorption layer component by weight is: cordierite 13-15 part, mullite 9-11 part, silochrom 6-8 part, montmorillonite 4-7 part, activated alumina 8-10 part, calcium sulfate 3-5 part, dimethicone 2-3 part, sodium alginate 3-4 part, monkey grass 3-5 Part, carbamide 2-3 part, silica gel 10-20 part, Kaolin 5-15 part, zeolite 6-10 part, aluminium oxide 1-5 part, aluminium glue 2-5 part, calcium oxide 1-3 part, zinc oxide 1-2 part, sesbania powder 1-3 part.
Irrigation the most according to claim 1 oozes HDPE tubing with micro-, it is characterised in that: described adsorption layer component by weight For: cordierite 14 parts, mullite 10 parts, silochrom 7 parts, montmorillonite 5 parts, activated alumina 9 parts, 4 parts of calcium sulfate, dimethyl Silicone oil 3 parts, sodium alginate 3 parts, monkey grass 4 parts, 3 parts of carbamide, 15 parts of silica gel, Kaolin 10 parts, 8 parts of zeolite, aluminium oxide 3 Part, aluminium glue 4 parts, calcium oxide 2 parts, zinc oxide 1 part, 2 parts of sesbania powder.
Irrigation the most according to claim 1 oozes HDPE tubing with micro-, it is characterised in that: the preparation method of described adsorption layer For:
A. aluminium glue, calcium oxide, zinc oxide, sesbania powder are taken, uniformly after mixing, through kneading, molding, pelletizing, primary drying, once Roasting, dipping, redrying, after baking obtain dehydrant；
B., silica gel is crossed 150 mesh sieves, and Kaolin crosses 200 mesh sieves, and zeolite crosses 80 mesh sieves, and aluminium oxide crosses 325 mesh sieves, the most successively will Silica gel, Kaolin, zeolite and the aluminium oxide mixing sieved, obtains adsorbent first product；
C. take cordierite, mullite, silochrom, montmorillonite, activated alumina, calcium sulfate, dimethicone, sodium alginate, Grind after monkey grass mixing, be then dried process, obtain adsorbent mixtures；
D. add distilled water after being mixed with the adsorbent mixtures obtained in step c by the adsorbent first product obtained in step b, put Enter in blender with rotating speed for the continuously stirred 30-45min of 1800r/min, obtain adsorbent, then the adsorbent obtained is added Dehydrant in step a, puts into and carries out drying operation in dehydrator, obtain adsorbing material, and adsorbing material i.e. prepares adsorption layer.
Irrigation the most according to claim 1 oozes HDPE tubing with micro-, it is characterised in that: it is distributed some on described adsorption layer Filter course, described filter course component by weight includes: pulverize coconut husk 20-25 part, zirconium oxide 5-8 part, micropowder silica gel 3-5 Part.
Irrigation the most according to claim 4 oozes HDPE tubing with micro-, it is characterised in that: the preparation method of described filter course For: coconut husk hot wash will be pulverized, soak 1-2 hour with 50-60% phosphoric acid solution the most at normal temperatures；Filter, take filtering residue Carbonization 1.5-2 hour in the retort of 550-600 DEG C, takes out；Mix with zirconium oxide, micropowder silica gel when temperature is down to room temperature Uniformly, add 60% sodium hydroxide and stir 1-1.5 hour, then filter taking-up；Clean 3-4 time with distilled water, drying.
CN201610762973.8A 2016-08-29 2016-08-29 A kind of irrigation oozes HDPE tubing with micro- Withdrawn CN106219789A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610762973.8A CN106219789A (en) 2016-08-29 2016-08-29 A kind of irrigation oozes HDPE tubing with micro-

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610762973.8A CN106219789A (en) 2016-08-29 2016-08-29 A kind of irrigation oozes HDPE tubing with micro-

Publications (1)

Publication Number Publication Date
CN106219789A true CN106219789A (en) 2016-12-14

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Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
CN (1) CN106219789A (en)

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Application publication date: 20161214

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