CN204111539U - The unitization module of one group of horizontal type structure - Google Patents

Abstract

The utility model relates to water treatment field; For problem be: how according to the feature of ozone and activated carbon depth-averaged model technique, design the unitization module of one group of horizontal type structure; The unitization module pile of this group horizontal type structure is got up, and is exactly the main framework that platform adopts the terminal water-treated prod of ozone and activated carbon depth-averaged model technique; In this main framework, embedding relevant auxiliary, the filtrate needed for loading, be the water treatment station that platform adopts ozone and activated carbon depth-averaged model technique, and technical indicator reaches China water purification project technological standard JB/T2032-1999; Due to the auxiliary embedded, the difference that the filtrate of loading can require according to raw water quality and user correspondingly adjusts, thus " the private customization " of product has been pushed to higher level.

Description

The unitization module of one group of horizontal type structure

Technical field

The utility model relates to water treatment field; For problem be: how according to the feature of ozone and activated carbon depth-averaged model technique, design the unitization module of one group of horizontal type structure; The unitization module pile of this group horizontal type structure is got up, and is exactly the main framework that platform adopts the terminal water-treated prod of ozone and activated carbon depth-averaged model technique; In this main framework, embedding relevant auxiliary, the filtrate needed for loading, be the water treatment station that platform adopts ozone and activated carbon depth-averaged model technique, and technical indicator reaches China water purification project technological standard JB/T2032-1999.

Background technology

The < China's economic Zhou Publications >2013 second phase, at " running water safety? " report in one literary composition: because water source is polluted, in 4467 waterworkss, the whole nation, the waterworks of 80% just can make Drinking water quality reach the requirement of 106 new national standards after only having and adopting ozone and activated carbon depth-averaged model technique; But up to the present, the whole nation only has the part of running water factory on the ground such as Beijing to adopt this technology, and they only account for about 2% of waterworks sum; Because the chronicity of Revegetation of Eco-environment, complicacy, arduousness and the fund that promotes waterworks water technology are come from where, be all a difficult problem, so want that allowing the common people open water tap just can directly drink, and wait decades!

For the water allowing the people of community resident and each enterprises and institutions drink safety and Health very soon, invention team of the present utility model, before this according to the feature of ozone and activated carbon depth-averaged model technique, invent the unitization module > (ZL 201420148875.6 of a < horizontal type structure; Application for a patent for invention numbers 2,014 1 0123558.9); This patented technology is applicable to build relatively large ozone and activated carbon depth-averaged model technique water treatment station, because: the various filtrate large usage quantities now comprising gac, recoil to them for convenience of daily, regenerate and change, this patent is specially provided with pre-treatment filtrate bucket and these two, main process filtrate bucket independently module in main framework.

For residential quarter and each enterprises and institutions, the very different in number: large unit, number is ten hundreds of, 100,000; Little unit, number tens people, hundreds of people; Because the quantity of subsection is extremely huge, so, be the water treatment station of the customized ozone and activated carbon depth-averaged model technique of subsection, have great meaning.

Summary of the invention

Invention the purpose of this utility model is: for building little miniature ozone and activated carbon depth-averaged model technique water treatment station, the unitization module of specialized designs one group of horizontal type structure ideally solves the healthy water problem of subsection personnel, and " the private customization " of product is pushed to higher level.

Realize the technical measures of the object of the invention as shown in Figure 1:

The unitization module of one group of horizontal type structure comprises: casing pond (1), casting bed stool (2), charcoal bed stool (3) and top cover of box (4);

Described casing pond (1), by cabinet exterior (11), bridge-type dividing plate (12), overflow wallboard (13), and No. two bridge-type dividing plates (14) compositions; And the height of overflow wallboard (13), lower than being in a bridge-type dividing plate (12) and No. two bridge-type dividing plates (14) in same level; And be in the height of a bridge-type dividing plate (12) and No. two bridge-type dividing plates (14) in same level, lower than the top of cabinet exterior (11);

The top of described cabinet exterior (11) side is provided with prosopyle (111), bottom is provided with discharge orifice (112) and air inlet port (113); On the lower sidely in the middle part of cabinet exterior (11) opposite side of correspondence be provided with water purification posticum (114);

The vessel space that described cabinet exterior (11) and a bridge-type dividing plate (12) are formed, is called pretreatment pool (A); The vessel space that a described bridge-type dividing plate (12) and overflow wallboard (13) are formed, is called ozone blast pool (B); The vessel space that described overflow wallboard (13) and No. two bridge-type dividing plates (14) are formed, is called ozone biological activated carbon pond (C); The vessel space that described No. two bridge-type dividing plates (14) and cabinet exterior (11) are formed, is called water purifying tank (D);

Described casting bed stool (2), is made up of the casting bed stool post (22) in the casting bed stool face (21) and support casting bed stool face that are covered with sieve aperture;

Described charcoal bed stool (3), is made up of charcoal bed stool post (32) in the charcoal bed stool face (31) and support charcoal bed stool face that are covered with sieve aperture;

It is characterized in that:

Described casting bed stool (2), on the base plate being placed in casing pond (1) corresponding to pretreatment pool (A); And the surrounding in casting bed stool face (21), the space between the surrounding of pretreatment pool (A) inwall corresponding thereto, is greater than 0 and is less than 2 millimeters; And the height in casting bed stool face (21), higher than the bottom plane of a bridge-type dividing plate (12);

Described charcoal bed stool (3), on the base plate being placed in casing pond (1) corresponding to ozone biological activated carbon pond (C); And the surrounding in charcoal bed stool face (31), the gap between the inwall surrounding in ozone biological activated carbon pond (C) corresponding thereto, is greater than 0 and is less than 2 millimeters; And the height in charcoal bed stool face (31), higher than the bottom plane of No. two bridge-type dividing plates (14);

Described top cover of box (4), on the top being placed in cabinet exterior (11).

For guaranteeing that product technology performance reaches the technological standard requirement of JB/T2032-1999, following LML formula should be followed, carries out the product design of being correlated with:

W/S < 10 meters/time and

H/ (W/S) > 12 minutes;

In formula: W---water purification max water yield (being obtained by simulation test)

The minimal design value of S---charcoal bed stool face (31) area

The minimal design value of H---carbon leaching material total height.

The beneficial effects of the utility model show: the main framework got up with the unitization module pile of one group of horizontal type structure, can structurally, and pretreatment pool, ozone blast pool, ozone biological activated carbon pond, water purification storage pool, four ponds are unified; Again can in technique, order except the pre-treatment of turbidity, and integrates the main process of the degree of depth of ozone sterilization, ozone oxidation, microbial film absorption, charcoal absorption, and the showdown process of optimizing water quality, the direct-connected straight button of three rings! So, only in this main framework, relevant auxiliary need be embedded, the filtrate needed for loading, be that platform adopts ozone and activated carbon depth-averaged model technique, and reach the water treatment station of China JB/T2032-1999 water purification project technological standard; Due to the auxiliary embedded, the difference that the filtrate of loading can require according to raw water quality and user correspondingly adjusts, thus " the private customization " of product has been pushed to higher level.

Below in conjunction with drawings and Examples in detail, technical scheme of the present invention is described in detail.

Accompanying drawing illustrates:

The unitization module of accompanying drawing 1 one groups of horizontal type structures;

The water treatment station of accompanying drawing 2 ozone and activated carbon depth-averaged model technique.

Description of reference numerals:

Casing pond (1), casting bed stool (2), charcoal bed stool (3), top cover of box (4);

Cabinet exterior (11), prosopyle (111), discharge orifice (112), air inlet port (113), water purification posticum (114), bridge-type dividing plate (12), overflow wallboard (13), No. two bridge-type dividing plates (14);

Pretreatment pool (A), ozone blast pool (B), ozone biological activated carbon pond (C), water purifying tank (D);

Casting bed stool face (21), casting bed stool post (22);

Charcoal bed stool face (31), charcoal bed stool post (32);

Float switch (M1); Backwash release valve (M2); Ozone input tube (M3); Take the device (M4) of water purification; Pre-treatment filtrate (N1); Main process filtrate gac (N2).

Embodiment

A standard quality-determining! The JB/T2032-1999 water purification project technological standard of China, will be applied in product design of the present invention.

(1) the unitization module > of the < mono-group of horizontal type structure shown in accompanying drawing 1, the method being assembled into the water treatment station > of the < ozone and activated carbon depth-averaged model technique shown in accompanying drawing 2 is very simple:

1., in the prosopyle (111) on the outer wall (11) of bucket pond (1), access the float switch (M1) be connected with tap water inlet channel; In earial drainage (112), connect backwash release valve (M2); In air inlet port (113), access ozone input tube (M3); In water purification posticum (114), connect the device (M4) of taking water purification;

2., on casting bed stool (2), load pre-treatment filtrate (N1);

3., on charcoal bed stool (3), process filtrate gac (N2) is become owner of in filling;

So far, with the main framework of the unitization module > pile of < mono-group of horizontal type structure, just become the water treatment station > of the < ozone and activated carbon depth-averaged model technique shown in accompanying drawing 2.

(2) water treatment technological process of the water treatment station > of the < ozone and activated carbon depth-averaged model technique shown in accompanying drawing 2 is:

Tap water====former water enters in pretreatment pool (A), and following current is filtered slowly from pre-treatment filtrate (N1), under let out in ozone blast pool (B), meanwhile remove turbidity, water is made to become clear====ozone of exposing to the sun in ozone blast pool (B), mix with pretreated aqueous phase, and sail against the current and overflow in ozone biological activated carbon pond (C), meanwhile ozone carries out sterilization and duplicate removal metal and organism====water following current in main process filtrate gac (N2) of being dissolved with ozone and filters slowly, then enter water purifying tank (D) from bottom, meanwhile carry out aerobic biologic membrane process and charcoal absorption, the various organism of powerful removal====obtained oxygen enrichment water purification is stored in water purifying tank (D) for subsequent use.

(3) the water treatment station > using method of the < ozone and activated carbon depth-averaged model technique shown in accompanying drawing 2 is:

User opens and closes the device (M4) of taking water purification at any time, just can obtain required water purification;

User regularly to active-carbon bed (N2) that only have a hundred or so kilogram weight, carries out manual cleaning and replacing, compared with now active-carbon bed with automatic backflushing, not only economizes charcoal but also economize on water, and profit is much larger than fraud.

(4) the water treatment station > of the < ozone and activated carbon depth-averaged model technique shown in accompanying drawing 2 in use, automatically do a little what?

The casing pond (1) of the water treatment station > of < ozone and activated carbon depth-averaged model technique is one and is divided into pretreatment pool (A), ozone blast pool (B), ozone biological activated carbon pond (C), water purification storage pool (D), the monoblock type communicating vessels in four case ponds that communicate; Their top water-level is the high-water that float switch (M1) is in, and now tap water water entry is closed by float switch (M1).

According to the principle of communicating vessels, when the device (M4) of taking water purification supplies water to user, the water purification water level be originally in the water purifying tank (D) of same horizontal plane is caused in capital, lower than the former water water level be stored in pretreatment pool (A); So under the action of gravity that former water produces at self potential energy, from first to last automatically complete all processes of whole water technology;

After said process ends at and closes and take the device (M4) of water purification, float switch (M1) is restored to high-water, and when closing tap water water entry;

Said process automated cycle endlessly.

(5) how the water treatment station > of the < ozone and activated carbon depth-averaged model technique shown in accompanying drawing 2, ensure that all technical reaches China JB/T2032-1999 water purification project technological standard and requires?

When in JB/T2032-1999, regulation is with charcoal absorption organism:

The velocity of flow of former water in active-carbon bed: V < 10 ms/h, 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 charcoal absorption organic time, so adopt the waterworks of ozone and activated carbon depth-averaged model technique both at home and abroad, all the flowing time of the former water dissolving in ozone in active-carbon bed, be revised as more than 12 minutes.Accordingly, the present invention, by following LML formula, carries out the design of product:

W/S < 10 meters/time (16.66 centimeters/minute) and

H/ (W/S) > 12 minutes

In formula: W---water purification max water yield (obtained by simulation test, accurately facilitate)

The minimal design value of S---charcoal bed stool face (31) area

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 S---charcoal bed stool face (31) area

The design load of the total height of H---carbon leaching material

The unit weight of M---carbon leaching material; According to active-carbon bed (N2) of measuring and calculating 100 kilogram weight, the unit that can be within 2000 people provides daily required drinking-water.

Technological innovation of the present invention, ozone and activated carbon depth-averaged model advanced technologies is adopted by providing for numerous medium and small miniature enterprises and institutions, technical indicator reaches JB/T2032-1999 requirement, effluent quality meets terminal water quality treater---the water treatment station of 106 new national standard requirements, thus be the safety and Health Drinking Water Problem that constituent parts solves employees as early as possible, provide Reliable guarantee.

Claims (2)

1. the unitization module of one group of horizontal type structure, comprises casing pond (1), casting bed stool (2), charcoal bed stool (3) and top cover of box (4);

Described casing pond (1), by cabinet exterior (11), bridge-type dividing plate (12), overflow wallboard (13), and No. two bridge-type dividing plates (14) compositions; And the height of overflow wallboard (13), lower than being in a bridge-type dividing plate (12) and No. two bridge-type dividing plates (14) in same level; And be in the height of a bridge-type dividing plate (12) and No. two bridge-type dividing plates (14) in same level, lower than the top of cabinet exterior (11);

The top of described cabinet exterior (11) side is provided with prosopyle (111), bottom is provided with discharge orifice (112) and air inlet port (113); On the lower sidely in the middle part of cabinet exterior (11) opposite side of correspondence be provided with water purification posticum (114);

The vessel space that described cabinet exterior (11) and a bridge-type dividing plate (12) are formed, is called pretreatment pool (A); The vessel space that a described bridge-type dividing plate (12) and overflow wallboard (13) are formed, is called ozone blast pool (B); The vessel space that described overflow wallboard (13) and No. two bridge-type dividing plates (14) are formed, is called ozone biological activated carbon pond (C); The vessel space that described No. two bridge-type dividing plates (14) and cabinet exterior (11) are formed, is called water purifying tank (D);

Described casting bed stool (2), is made up of the casting bed stool post (22) in the casting bed stool face (21) and support casting bed stool face that are covered with sieve aperture;

Described charcoal bed stool (3), is made up of charcoal bed stool post (32) in the charcoal bed stool face (31) and support charcoal bed stool face that are covered with sieve aperture;

It is characterized in that:

Described casting bed stool (2), on the base plate being placed in casing pond (1) corresponding to pretreatment pool (A); And the surrounding in casting bed stool face (21), the space between the surrounding of pretreatment pool (A) inwall corresponding thereto, is greater than 0 and is less than 2 millimeters; And the height in casting bed stool face (21), higher than the bottom plane of a bridge-type dividing plate (12);

Described charcoal bed stool (3), on the base plate being placed in casing pond (1) corresponding to ozone biological activated carbon pond (C); And the surrounding in charcoal bed stool face (31), the gap between the inwall surrounding in ozone biological activated carbon pond (C) corresponding thereto, is greater than 0 and is less than 2 millimeters; And the height in charcoal bed stool face (31), higher than the bottom plane of No. two bridge-type dividing plates (14);

Described top cover of box (4), on the top being placed in cabinet exterior (11).

2. the unitization module of one group of horizontal type structure described in claim 1, is characterized in that:

For guaranteeing that product technology performance reaches the technological standard requirement of JB/T2032-1999, following LML formula should be followed, carries out the product design of being correlated with:

W/S < 10 meters/time and

H/ (W/S) > 12 minutes;

In formula: W---water purification max water yield (being obtained by simulation test)

The minimal design value of S---charcoal bed stool face (31) area

The minimal design value of H---carbon leaching material total height.