CN203866149U - Modularized module adopting horizontal structure - Google Patents
Modularized module adopting horizontal structure Download PDFInfo
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- CN203866149U CN203866149U CN201420148675.6U CN201420148675U CN203866149U CN 203866149 U CN203866149 U CN 203866149U CN 201420148675 U CN201420148675 U CN 201420148675U CN 203866149 U CN203866149 U CN 203866149U
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Abstract
The utility model discloses a modularized module adopting a horizontal structure, which is designed by aiming at characteristics of an ozonic biological active carbon deep water treatment technology. The modularized module comprises a barrel tank (1), a pre-treatment filter material barrel (2), a main treatment filter material barrel (3) and a barrel tank cover (4), wherein the barrel tank (1), the pre-treatment filter material barrel (2), the main treatment filter material barrel (3) and the barrel tank cover (4) are stacked together to form a main framework of a terminal water treatment product; related auxiliaries are inserted, and required filter materials are loaded in the main framework to form the terminal water treatment device adopting the ozonic biological active carbon deep water treatment technology.
Description
Technical field
The present invention relates to water treatment field; The problem solving is: how, for the feature of ozone biological activated carbon degree of depth water technology, the unitization module of a set of horizontal type structure that design makes new advances, gets up their piles, is exactly the main framework of station terminal water-treated prod; In this main framework, embed relevant auxiliary, pack required filtrate into, be a terminal water quality treater that adopts ozone biological activated carbon degree of depth water technology.
Background technology
When the water source of tap water is one, two class water quality, terminal water processor adopts the gac water-purifying process of ozone sterilization type, is the most applicable; When the water source of tap water is three class water quality, terminal water processor adopts ozone biological activated carbon advanced treatment process, is only the most applicable.
" the unitization module of a set of horizontal type structure ", is applicable to adopt the terminal water-treated prod exploitation of the gac water-purifying process of ozone sterilization type.While adopting the gac water-purifying process of ozone sterilization type, first to carry out ozone pre-oxidation, now, ozone be exposed to the sun and is arranged in the former pond of top, then be dissolved in the ozone in former water, along with former water goes downstream from pre-treatment filter bed; Then, from active-carbon bed bottom, sail against the current ... ..; From start to finish all bringing into play the sterilization of ozone and antibacterial effect.
Above-mentioned flow process, it is improper indiscriminately imitating in ozone biological activated carbon advanced treatment process; Reason is that the Main Function of ozone is sterilization in the gac water-purifying process of ozone sterilization type, to guarantee that gac can extremely not change because growing bacterium.
In ozone biological activated carbon advanced treatment process, the Main Function of ozone is to remove organism; With ozone sterilization by comparison, add the time of ozone longer, add the concentration of ozone larger; If indiscriminately imitated, will be difficult to reach the requirement of ozone biological activated carbon degree of depth water technology, treatment effect is not good.
Now, correct way: the one, ozone is directly added in the former water after pre-treatment filter bed is processed, the 2nd, allow and add the water after ozone, from active-carbon bed top, go downstream.
According to < China's economic Zhou Publications > (second phase in 2013) at " running water safety? " in one literary composition, report: there is more than 4000 waterworks in the whole nation, 80% waterworks only has the ozone of employing biological activated carbon advanced treatment process, just can make the to dispatch from the factory index of water quality, reaches the new national standard requirement of 106; Because where money is from being a hang-up, so a senior professor thinks: want to open water tap and just can directly drink, at least also obtain 30 years!
Adopt the terminal water treatment of ozone biological activated carbon degree of depth water technology, can allow people drink the water of safety and Health at once, do not need to wait again it 30 years! As can be seen here, adopt the terminal handler of ozone biological activated carbon depth water science and engineering skill, have how important value and significance!
Summary of the invention
Goal of the invention of the present invention is: for the feature of ozone biological activated carbon degree of depth water technology, specialized designs goes out a kind of unitization module of horizontal type structure, solve the issues for product development of the terminal water quality treater that adopts ozone biological activated carbon degree of depth water technology, the level of product " private customization ", push a Xin Bands section to.
Beneficial effect of the present invention shows, a kind of unitization module of horizontal type structure, can be structurally, pretreatment box, filter bed case, clear water tanks, these three casings are integrated, again can be in water technology, make the core processing of the filter bed that the pre-treatment of turbidity removal, biological adsorptivity function have both, the optimizing water quality showdown that can carry out in clear water tanks process, these three process procedures staple together; " kill two birds with one stone ", guarantee the perfection performance of water treatment station treatment function.
The general thought that realizes the object of the invention is: " the unitization module of a set of horizontal type structure " (application for a patent for invention number: 201410119188.1 that is applicable to the gac water-purifying process of ozone sterilization type; Utility application number: 201420143285.X) transform according to the requirement of ozone biological activated carbon degree of depth water technology, make it to meet following requirement: the one, ozone is directly added in the former water after pre-treatment filter bed is processed, the 2nd, allow and add the water after ozone, from active-carbon bed top, go downstream.
Realize the technical measures of general thought of the present invention, as shown in Figure 1: with " the unitization module of a set of horizontal type structure " by comparison, it is a many stifled overflow wallboard (13); With it, both sealed the water route that a bridge-type dividing plate (12) leads to main processing filtrate bucket (3) bottom, and again current had been stopped, the last top from oneself overflows to the top of main processing filtrate bucket (3); Meanwhile, also solved ozone has directly been added to the problem in the former water after pre-treatment filter bed is processed, because when embedding auxiliary, only need, the aeration stone of ozonizer, insert the top of main processing filtrate bucket (3).
A kind of unitization module of horizontal type structure comprises: bucket pond (1), pre-treatment filtrate bucket (2), main processing filtrate bucket (3), bucket Chi Gai (4);
Described bucket pond (1), is comprised of outer wall (11), a bridge-type dividing plate (12), overflow wallboard (13) and No. two bridge-type dividing plates (14); And the height of overflow wallboard (13), lower than the outer wall in same level (11), a bridge-type dividing plate (12) and No. two bridge-type dividing plates (14);
The top that one side inwall of described outer wall (11) is provided with groove 1 (111), outer wall (11) is provided with positioning table (112), be positioned at former water intakes that the bottom of a side outer wall (11) is provided with discharge orifice 1 (113), the bottom that is positioned at water purification water outlet one side outer wall (11) is provided with discharge orifice 2 (114);
A described bridge-type dividing plate (12) is towards a side of outer wall (11), be provided with groove 2 (121), and groove 2 (121) on same horizontal plane, forms the support platform to pre-treatment filtrate bucket (2) with groove 1 (111) jointly;
Interval between a described bridge-type dividing plate (12) and overflow wallboard (13), is referred to as overflow ducts;
Described overflow wallboard (13), towards a side of No. two bridge-type dividing plates (14), is provided with groove 3 (131);
Described No. two bridge-type dividing plates (14), towards a side of overflow wallboard (13), are provided with groove 4 (141); And groove 4 (141) on same horizontal plane, forms the support platform to main processing filtrate bucket (3) with groove 3 (131) jointly;
Space between described No. two bridge-type dividing plates (14) and outer wall (11) is called clear water tanks;
On the barrel soleplate of described pre-treatment filtrate bucket (2), be covered with sieve aperture 1 (21), its barrel of top is provided with locating dowel 1 (22);
On the barrel soleplate of described main processing filtrate bucket (3), be covered with sieve aperture 2 (31), its barrel of top is provided with locating dowel 2 (32);
It is characterized in that:
Described pre-treatment filtrate bucket (2), by the locating dowel 1 (22) on its barrel of top, piles up in the groove 1 (111) by outer wall (11) and the common support platform forming of the groove on bridge-type dividing plate (12) 2 (121);
Described main processing filtrate bucket (3), by the locating dowel 2 (32) on its barrel of top, pile up the groove 3 (131) at overflow wallboard (13), and the groove 4 (141) of No. two bridge-type dividing plates (14), in the common support platform forming;
Described bucket Chi Gai (4), it is lower to being placed on the positioning table (112) on outer wall (11) top.
Below in conjunction with drawings and Examples in detail, technical scheme of the present invention is described in detail.
Accompanying drawing explanation:
The unitization module of 1 one kinds of horizontal type structures of accompanying drawing;
The water treatment station of accompanying drawing 2 ozone biological activated carbon degree of depth water technologies.
Description of reference numerals:
Bucket pond (1)
Outer wall (11) groove 1 (111) positioning table (112)
Discharge orifice 1 (113) discharge orifice 2 (114);
A bridge-type dividing plate (12) groove 2 (121);
Overflow wallboard (13) groove 3 (131);
No. two bridge-type dividing plates (14) groove 4 (141);
Pre-treatment filtrate bucket (2) sieve aperture base plate 1 (21) locating dowel 1 (22);
Main processing filtrate bucket (3) sieve aperture base plate 2 (31) locating dowels 2 (32);
Bucket Chi Gai (4);
Backwash filtrate release valve (F1) variable frequency water supply pump (F2) pre-treatment filtrate (F3)
Main processing filtrate (F4) float switch (F5) ozonizer (F6).
The L M L theory that innovation team of the present invention creates, i.e. the mathematical model of guide product exploitation is: the prerequisite of giving full play to active micropore filtration " except misfortune is stayed treasured " effect is: amounts of activated carbon is sufficient, water technology is complete; Sufficient condition is: slow filter, charcoal bed do not harden.
The national machinery industry technological standard of giving full play to activated carbon capillary filtration " except misfortune is stayed treasured " effect is: JB/T2032-1999.
" standard quality-determining ", has high standard, just has high quality! The product that application the present invention designs, strictly follows the requirement of national this technological standard of JB/T2032-1999.
Embodiment
(1), the unitization module > of an accompanying drawing 1< horizontal type structure, the method that is assembled into the water treatment station > of accompanying drawing 2< ozone biological activated carbon degree of depth water technology is:
1. the discharge orifice on the outer wall (11) of bucket pond (1) 1 (113) is upper, connects backwash filtrate release valve (F1); Upper at discharge orifice 2 (114), connect the variable frequency water supply pump (F2) of taking water purification;
2. in pre-treatment filtrate bucket (2), be packed into pre-treatment filtrate (F3);
3. in main processing filtrate bucket (3), filling is become owner of and is processed filtrate (F4);
4. on bucket Chi Gai (4), set respectively into:
4-1. float switch (F5); The water inlet pipe of float switch (F5) its ball float that is connected with running water pipe will swim in the former water of pre-treatment filtrate (F3) top;
4-2. ozonizer (F6); Its ozonation aerated stone will fall in the water of main processing filter (F4) top;
(2) its water treatment technological process of water treatment station > of the < ozone biological activated carbon degree of depth water technology shown in accompanying drawing 2 is:
The following current in pre-treatment filtrate bed of tap water---former water is filtered slowly, go turbidity, water to become that clear water following current in main processing filtrate bed is filtered slowly---in the water that ozone is exposed to the sun above main processing filtrate bed---, carry out on the one hand microbial film processing, carry out on the one hand main processing filtrate adsorption treatment---the water purification making is stored in clear water tanks.
(3) the water treatment station > using method of the < ozone biological activated carbon degree of depth water technology shown in accompanying drawing 2 is:
User opens and closes the clear water faucet being connected with variable frequency water supply pump (F2) water supply line at any time, just can obtain required water purification.
(4) the water treatment station > of the < ozone biological activated carbon degree of depth water technology shown in accompanying drawing 2 in use, automatically done a little what?
The bucket pond (1) of the water treatment station > of < ozone biological activated carbon degree of depth water technology is an all-in-one-piece communicating vessels, its top water-level be float switch (F5) in high-water, and close in tap water water entry.
According to the principle of communicating vessels, when variable frequency water supply pump (F2) supplies water to user, all can cause the water purification water level in same horizontal plane originally, lower than the former water water level that is stored in pre-treatment filtrate (F3) top; So under the action of gravity that former water produces at self potential energy:
First from pre-treatment filtrate (F3) the slow filter of following current and under, meanwhile, the silt in water, iron rust, colloid are held back, to protect main processing filtrate (F4) not because Shou Wu Minus is imitated;
Former water after turbidity removal is returned clearly through pre-treatment filtrate (F3), owing to being subject to stopping of overflow wallboard (13), and along the overflow ducts cross flow that makes progress; Until overflow into the top of main processing filtrate (F4) from the top of overflow wallboard (13); Meanwhile, ozonizer (F6) exposes to the sun ozone in water;
And then the former water that is dissolved with ozone goes downstream from the top of main processing filtrate (F4), until flow out from the bottom of main processing filtrate (F4); Meanwhile, there are two kinds of main operations:
The one, ozone supports and is attached to the aerobic biologic membrane on gac top layer, the organism in efficient adsorption water; The 2nd, the nanofiltration function of gac performance self millipore filtration, i.e. the objectionable impuritiess such as adsorb organic compound, heavy metal, chlorine residue, and allow the without hindrance and mistake of the benefit materials such as mineral substance;
Whole process ends at float switch (F5) in high-water, and closes in tap water water entry.
(5) how the water treatment station > of the < ozone biological activated carbon degree of depth water technology shown in accompanying drawing 2 guarantees its all technical, reach the requirement of national machinery industry technological standard JB/T2032-1999?
When in machinery industry standard JB/T2032-1999, regulation is with charcoal absorption organism:
The velocity of flow of former water in active-carbon bed: 10 ms/h of V <, and
The flowing time of former water in active-carbon bed: T > 6 minutes
Owing to giving full play to the organic time in microbial film planar water, be far longer than the organic time of charcoal absorption, so insider both domestic and external is according to the practical experience of oneself, mostly the flowing time in active-carbon bed the former water that dissolves in ozone, is revised as more than 12 minutes.Accordingly, the present invention will, by following LML formula 2, carry out the design of product:
10 meters of W/S </time (16.66 centimeters/minute) and
H/ (W/S) > 12 minutes
In formula: W---variable frequency water supply pump max water yield (choosing pump size by demand);
The minimal design value of the main processing filtrate of S---bucket (3) floorage
The minimal design value of H---carbon leaching material total height.
The loadings N of carbon leaching material, can be calculated as follows acquisition:
N＝S*H*M
In formula: the design load of the main processing filtrate of S---bucket (3) floorage
The design load of the total height of H---carbon leaching material
The unit weight of M---carbon leaching material.
For wanting to build the problem that water treatment station solves worker health drinking-water, constituent parts is the water treatment station > of the < ozone biological activated carbon degree of depth water technology shown in 2 completely with reference to the accompanying drawings, utilize LML formula, oneself just can design and build the personalized water treatment station that is suitable for our unit's use, and faster and better, economic and practical, inexpensive! Because the bucket pond (1) in the water treatment station > of the < ozone biological activated carbon degree of depth water technology shown in accompanying drawing 2, constituent parts has the ability by the structure of Steel Concrete, it to be built completely; At most pre-treatment filtrate bucket (2) is become to stainless steel structure with main processing filtrate bucket (3) external processing and oneself.
Be not difficult to find out: technological innovation of the present invention, for each unit does it yourself to solve a difficult problem that oneself drinks safety and Health water, the strong guarantee providing.
Claims (1)
1. the unitization module of a horizontal type structure comprises: bucket pond (1), pre-treatment filtrate bucket (2), main processing filtrate bucket (3), bucket Chi Gai (4);
Described bucket pond (1), is comprised of outer wall (11), a bridge-type dividing plate (12), overflow wallboard (13) and No. two bridge-type dividing plates (14); And the height of overflow wallboard (13), lower than the outer wall in same level (11), a bridge-type dividing plate (12) and No. two bridge-type dividing plates (14);
The top that one side inwall of described outer wall (11) is provided with groove 1 (111), outer wall (11) is provided with positioning table (112), be positioned at former water intakes that the bottom of a side outer wall (11) is provided with discharge orifice 1 (113), the bottom that is positioned at water purification water outlet one side outer wall (11) is provided with discharge orifice 2 (114);
A described bridge-type dividing plate (12) is towards a side of outer wall (11), be provided with groove 2 (121), and groove 2 (121) on same horizontal plane, forms the support platform to pre-treatment filtrate bucket (2) with groove 1 (111) jointly;
Interval between a described bridge-type dividing plate (12) and overflow wallboard (13), is referred to as overflow ducts;
Described overflow wallboard (13), towards a side of No. two bridge-type dividing plates (14), is provided with groove 3 (131);
Described No. two bridge-type dividing plates (14), towards a side of overflow wallboard (13), are provided with groove 4 (141); And groove 4 (141) on same horizontal plane, forms the support platform to main processing filtrate bucket (3) with groove 3 (131) jointly;
Space between described No. two bridge-type dividing plates (14) and outer wall (11) is called clear water tanks;
On the barrel soleplate of described pre-treatment filtrate bucket (2), be covered with sieve aperture 1 (21), its barrel of top is provided with locating dowel 1 (22);
On the barrel soleplate of described main processing filtrate bucket (3), be covered with sieve aperture 2 (31), its barrel of top is provided with locating dowel 2 (32);
It is characterized in that:
Described pre-treatment filtrate bucket (2), by the locating dowel 1 (22) on its barrel of top, piles up in the groove 1 (111) by outer wall (11) and the common support platform forming of the groove on bridge-type dividing plate (12) 2 (121);
Described main processing filtrate bucket (3), by the locating dowel 2 (32) on its barrel of top, pile up the groove 3 (131) at overflow wallboard (13), and the groove 4 (141) of No. two bridge-type dividing plates (14), in the common support platform forming;
Described bucket Chi Gai (4), it is lower to being placed on the positioning table (112) on outer wall (11) top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420148675.6U CN203866149U (en) | 2014-03-31 | 2014-03-31 | Modularized module adopting horizontal structure |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420148675.6U CN203866149U (en) | 2014-03-31 | 2014-03-31 | Modularized module adopting horizontal structure |
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| Publication Number | Publication Date |
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| CN203866149U true CN203866149U (en) | 2014-10-08 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420148675.6U Expired - Fee Related CN203866149U (en) | 2014-03-31 | 2014-03-31 | Modularized module adopting horizontal structure |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104944675A (en) * | 2014-03-31 | 2015-09-30 | 刘德周 | Building block type modules of horizontal structure capable of continuous downstream filtration |
| CN112875989A (en) * | 2021-01-21 | 2021-06-01 | 贵州师范大学 | Drinking water purification device convenient to karst mountain area dispersion peasant household uses |
-
2014
- 2014-03-31 CN CN201420148675.6U patent/CN203866149U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104944675A (en) * | 2014-03-31 | 2015-09-30 | 刘德周 | Building block type modules of horizontal structure capable of continuous downstream filtration |
| CN112875989A (en) * | 2021-01-21 | 2021-06-01 | 贵州师范大学 | Drinking water purification device convenient to karst mountain area dispersion peasant household uses |
| CN112875989B (en) * | 2021-01-21 | 2022-11-29 | 贵州师范大学 | Drinking water purification device convenient to karst mountain area dispersion peasant household uses |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141008 Termination date: 20210331 |
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| CF01 | Termination of patent right due to non-payment of annual fee |