CN104071937B - Catalyst intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external - Google Patents

Abstract

The present invention relates to a kind of catalyst and intercept the High-capacity photocatalytic wastewater degradation device that mechanism is external, belong to technical field of waste water processing.In existing correlation technique, there is microwave energy waste, single tank wastewater treatment capacity is less than normal, degradation reaction terminal moment difficulty is distinguished, agglomeration thing cannot strength dissipates in situ, agglomeration occurs immediately to be perceived etc. problem, and this case is for above-mentioned series of problems.Its structure limits microwave irradiation spatial domain, it is allowed to reactor significantly dilatation；Its structure also intercepts catalyst step by step with the back flush type filter of external multi-stage cascade；Its structure low-frequency ultrasonic waves dissipation agglomeration thing, incidentally clean quartz ampoule simultaneously；Its structure also automatic immediate can close line related when degrading terminal；Its structure also can warn agglomeration to be inclined to.

Description

Catalyst intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external

Technical field

The present invention relates to a kind of catalyst and intercept the High-capacity photocatalytic wastewater degradation device that mechanism is external, belong to C02F waste water and process Technical field.

Background technology

Microwave and photo catalysis degradation treatment technology, as a kind of effective for the harmless treatment skill containing organic pollution industrial wastewater Art, the most interesting.

About microwave and photo catalysis degradation technique, as an example, may refer to the Chinese patent Shen of Publication No. CN102260003A Please case.

The disclosure number is the Chinese patent application case of CN102260003A, is using microwave as excitaton source, excites electrodeless ultraviolet lamp Launching ultraviolet, irradiate the suspension mixed with photochemical catalyst titanium dioxide in liquid internal, this electrodeless ultraviolet lamp is by quartz ampoule institute cage Cover protects, and is free air pump persistently to inject air to this quartz ampoule inner chamber, quartz cavity the air overflowed via pipeline be positioned at anti- Answering the micro porous aeration head UNICOM bottom device, the lower zone of this inside reactor is aeration zone, the upper area of this inside reactor Being microwave and photo catalysis reaction zone, the program also with the membrane separation assemblies that reactor is built-in, carries the water after analysis purifies, and with this film Separation assembly realizes retaining of photochemical catalyst titanium dioxide fine particles and uses；The program also non-polar ultraviolet light source and membrane separation assemblies it Between set up dividing plate, for preventing the ultraviolet radiation injury to organic membrane separation assemblies；It is passed through the air of inside reactor, Part the most directly participates in relying on the photocatalytic degradation of photochemical catalyst titanium dioxide to react, some air, direct at ultraviolet light Under irradiation, generating a certain amount of ozone, the ozone of this generation the most also plays the direct oxidative degradation for organic pollution Effect.

The disclosure number is that the Chinese patent application case of CN102260003A is certainly for microwave and photo catalysis wastewater degradation technology Progress serves very important impetus, and the work that its research staff is launched in this field is admirable.

Meaning based on sincere admiration, and, common striving direction, to be talked below us is problem.

The problem below will spoken of, has 14；These 14 problems are arranged side by side 14 problems；The priority of its sequence Consider easily merely for the sake of discussing.

One of problem:

The disclosure number is the Chinese patent application case of CN102260003A, and it divides for the film intercepting catalyst titanium dioxide fine particles It is to be placed in reactor inner chamber from assembly, is immersed among process object liquid, and relies on washing away containing ozone bubbles of ascension Membrane separation assemblies, the institute's catalyst particles that adsorbs, be detained that thereby removes its surface, reach the recovery of catalyst particles, recycling Purpose, meanwhile, it is self-cleaning and keep its separating power that membrane separation assemblies is also dependent on this mode, then, based on this structure, only Business curtain hollow fiber film assembly or plate film assembly can be selected, and, this membrane separation assemblies is to need to be immersed in ozone In the context of the strong oxidizing property of bubble ascension, therefore, the tolerance against oxidative power of membrane separation assemblies is necessarily required, common material The organic film separation assembly of matter is not resistant to such use environment, therefore can only select the membrane separation assemblies of PVDF material, this Point clearly illustrates in the 0009th section of word of this case disclosure and claim 3；This kind needs special tolerance against oxidative power Its material of filter membrane is relatively costly, and its commercially available price is certainly also above common organic micro-filtration membrane module of non-oxidation durability requirements；Change Sentence is talked about, and the frame mode of this case causes the material of membrane separation assemblies to be limited to PVDF material costly.Further, dress Putting interior possible ultraviolet light to reveal, may touch organic film assembly, this organic film assembly material also required that in device can be resisted Ultraviolet light irradiation, from the point of view of this, organization plan based on this device, the material of organic film separation assembly also can only be limited in PVDF material costly.

Organic film assembly, compared to ceramic filter assemblies, has its obvious advantage；About this point, special for filtering technique For the personage of industry, it is known, does not the most launch to repeat.

So, under the premise using organic material membrane module, this PVDF filter membrane material limitation can be bypassed？This is One needs the problem solved, and this is one of problem.

The two of problem:

In view of scouring force, the cleaning capacity of described ascension bubble are more weak, therefore, with this cleaning mode with the use of UF membrane The filter opening aperture of bigger micro-filtration rank can only be selected in its aperture of assembly, and the filter opening aperture of this micro-filtration rank is 0.1-0.2 micron, About this point, have in the 0009th section of word of this case disclosure and claim 3 equally and clearly limit, this kind of filter opening aperture Limit, from the type selecting of the such membrane separation assemblies of this case, built-in and soak from the point of view of occupation mode, the self-cleaning method of ascension bubble, be Inevitable, its filter opening aperture can only be limited in micro-filtration rank.In other words, this in the way of ascension bubble washes away its scouring force, Cleaning force is the most weak, to such an extent as to cannot tackle the filter membrane of more small-bore at all, and thus, in this case device, filter sizes limits Between 0.1 micron-0.2 micron, it it is the inevitable choice not discussing leeway.

The filter opening aperture of so-called 0.1-0.2 micron, if changing a measurement unit, corresponding is exactly the filter opening hole of 100-200 nanometer Footpath；That is any concept？For 100 nanometer filter opening apertures of its lower limit, its size of catalyst particles that it can intercept Must be more than 100 nanometers, and cannot be intercepted less than the catalyst particles of 100 nanometers；In other words, less than 100 The catalyst particles of nanometer by being directed through, by the filter opening of membrane module, be mixed into so-called water purification that degradation reaction device exported it In.

Need now to have a talk the particle diameter of photochemical catalyst involved by ultraviolet catalytic degradation reaction and photochemical catalyst dosage form selection.

The professional person being engaged in photocatalytic degradation research both knows about, and reacts with the photochemical degradating of uv light induction, and its catalyst is many Select titanium dioxide fine particles catalyst；At present, laboratory level has been developed for various in style urging based on titanium-dioxide photo Changing the light degradation particle catalyst of characteristic, certainly, the light degradation catalyst that these different preparation methods are formed, its particle diameter is also It is various；Its particle diameter of photochemical catalyst that different preparation methods are made is little to 20 nanometers, greatly to 100000 nanometers namely 100 microns, Have, be wherein no lack of the photochemical catalyst kind of excellent performance；But, due to performance long-time stability evaluate, preparation cost and The restriction of market expansion etc. aspect factor, most of its deliverability of described photochemical catalyst is limited only to laboratory level, And do not have to form the most commercially available level of production；The most known can make a big purchase in large quantities commercially available can be actual a large amount of The photochemical catalyst for ultraviolet light wave band used is famous gas phase titanium dioxide P25；Its concrete skill of gas phase titanium dioxide P25 Art implication, insider both knows about, and does not the most launch to repeat；The average grain diameter of gas phase titanium dioxide P25 is 21 nanometers；Gas Phase titanic oxide P25 performance not very optimum, but, its stable performance, it is important to can commercially make a big purchase in large quantities and obtain, and Can use the most in a large number, therefore, the most usually be used as weighing respectively with P25 catalyst in photocatalysis specialized laboratory Plant reference pointer or the contrast pointer of self-made photocatalyst catalytic performance, it is true that in view of the feature of ultraviolet catalytic degradation reaction, The photochemical catalyst that decentralization is the highest, is suitable for the needs of this type reaction, say, that average grain diameter is at the light of 21 ran Catalyst its catalyst interfacial area that can provide, anti-settling ability, catalytic performance long-time stability etc. aspect, comprehensive and Speech, is optimal.Simply, at present, good and cheap, it is possible to the actual ready-made commercially available business making a big purchase in large quantities, using The photochemical catalyst of the ultraviolet light wave band of grade, it is simply that average grain diameter is the gas phase titanium dioxide P25 catalyst of 21 nanometers；In industry The application of scale, this average grain diameter be the photochemical catalyst of 21 nanometers be actual first-selection.

Already described above and, the disclosure number is the Chinese patent application case of CN102260003A, and it is for intercepting the film of photochemical catalyst Assembly, is the catalyst particles that stripping film assembly surface adsorbs, deposits that washes away with ascension bubble, but, this kind is to rise Rise its scouring force of mode that bubble washes away, cleaning force the most weak, to such an extent as to the filter membrane of more small-bore cannot be tackled at all, therefore, In this case device, filter sizes is limited at micro-filtration filter opening rank between 0.1 micron-0.2 micron, for changing a measurement unit, In this case device, filter sizes is limited at the micro-filtration filter opening rank between 100 nanometer-200 nanometers, and this is not discuss leeway Inevitable choice；This case certainly cannot intercept as above flat without the micro-filtration filter opening between selectable 100 nanometer-200 nanometers All particle diameters are the gas phase titanium dioxide P25 particle of 21 nanometers；So, if using P25 photochemical catalyst, this catalyst will completely Cannot intercept, and flow in so-called water purification, form secondary pollution, certainly also result in the heavy losses of catalyst and unrenewable； Even if using the titanium dioxide optical catalyst of the big particle diameter special for this of other kind, it collides because of mutual during using Or collide with wall, inevitable also can produce a large amount of small particle fragment, wherein particle diameter is less than the fragment of 100 nanometers, equally can not be by Micro-filtration filter opening between 100 nanometer-200 nanometers is intercepted, these fractionlets also can through its membrane module enter so-called water purification it In, form secondary pollution.

Visible, the disclosure number is the Chinese patent application case of CN102260003A, and it is for the interception structure of photochemical catalyst particulate The cleaning solution of scheme and related film assembly is the most undesirable.

Therefore, how under the premise of this case advantage of incorporating things of diverse nature, reach the fine interception for photochemical catalyst particulate and return Receiving use again, be a important topic the most worth thinking deeply about, this is the two of problem.

The three of problem:

It is known that liquid water body itself also is able to absorb the energy of microwave, and cause the liquid water body that is processed itself Temperature-rise effect, and this with wastewater treatment process the temperature-rise effect that occurs, be not the most our situation of being expected, in other words Saying, the microwave energy from magnetron is used for exciting electrodeless ultraviolet lamp the most completely, and has quite a few should be served only for swashing The microwave energy sending out electrodeless ultraviolet lamp is dissipated in described temperature-rise effect, and it is unnecessary that the temperature-rise effect that this kind is not fond of causes Microwave energy waste, in view of disclosed above number be CN102260003A the apparatus structure side that shown of Chinese patent application case Case, its rational approach, can only be to reduce single tank process capacity in other words by the volume of minimizing microwave and photo catalysis reactor to come Reach the purpose weakening the unnecessary dissipation of microwave, about this point, in this its detailed description of the invention of CN102260003A application case Clearly have expressed the suitable size overall about this apparatus structure, what its expressed preferred size was corresponding is exactly that a profile is the least Device, then, consequently, it is possible to the distance of reactor wall and microwave radiation source is little, the wastewater flow rate contacted with microwave is little, The microwave energy that waste water is absorbed is the least, corresponds ground, and the wastewater treatment capacity of single tank is the least, more specifically Ground is said, the internal capacity corresponding to device suitable size expressed in embodiment is 40 liters, namely single tank wastewater treatment capacity is 40 liters, i.e. 0.04 cube, in other words, its once a complete set of, substantial length of operation solve only the industrial wastewater of 0.04 cube, then, Being accomplished by the repetition operated by a complete set of head to tail carried out many times, the cumulative of its treating capacity just has plant-scale meaning, So to say, the most individual analogy substantially, 0.04 cube of such waste water of single tank that its preferred structure size of this case is generally corresponding to Treating capacity, need to repeat 1000 times by a complete set of head to tail, substantial length of operation, its accumulation amount, can be only achieved 40 cubes such one Individual have industrial level wastewater treatment capacity, the most loaded down with trivial details repeating will cause the serious waste of human and material resources, Visible, the wastewater degradation treatment effeciency of its reality of scheme that this kind is shown by CN102260003A may not be fully up to expectations. Therefore, how on the premise of not causing the waste of more microwave energy or reducing microwave energy waste, increase single tank wastewater treatment capacity, Reduce this batch (-type) wastewater treatment equipment unnecessary too many and repeated number of times by head to tail, improve its waste water and process effect Rate, is a significant technical problem merited attention.

On the other hand, according to the literature, some system, in the case of microwave direct irradiation wastewater liquid, photochemical catalysis is dropped Solve efficiency and truly have raising, say, that in some system, between microwave direct irradiation wastewater liquid and photochemical catalysis degraded, There is certain coupling.

Therefore, how on the premise of taking into account described coupling, improve the treatment effeciency of wastewater degradation device, be worth inquiring into, This is the three of problem.

The four of problem:

The scheme that this kind is shown by CN102260003A, the bubble of the internal unrestrained cloth ascension of its retort, for driving a reaction tank The shuttling movement of the relatively large yardstick of internal liquid, contributes the most inadequate；Certainly, this weak point, for CN102260003A In scheme such as its detailed description of the invention the fact that clear expression for upper corresponding small size, low capacity device, almost without what Observable impact.From the point of view of plant-scale application demand, undersized can not the device of divergence process amount certainly the most much Attraction；So, as a kind of possibility, if there being certain mode to be capable of the significantly expansion for the treatment of capacity, under this situation, Its importance of shuttling movement of the relatively large yardstick of retort internal liquid will highlight naturally；Imagine the most this process The possibility that amount is significantly expanded, then, how to strengthen the shuttling movement of the relatively large yardstick of retort internal liquid, be certainly exactly Individual problem, this is the four of problem.

The five of problem:

For the photochemical catalysis oxidation reaction of ultraviolet light wave band, this kind of oxidation is anti-to have the most several following key element to influence whether The efficiency answered, first ultraviolet wavelength, intensity, it two is photochemical catalyst in the particle diameter of photochemical catalyst, unit volume reactant liquor Usage amount, himself catalytic performance etc. of photochemical catalyst, it three is organic concentration in oxidized object i.e. water body, has Oxidation complexity that machine thing molecular structure is determined himself etc., it four is the sufficient degree of oxygen atmosphere, in other condition In the case of identical, the sufficient degree of oxygen atmosphere, will become and affect an act foot of photochemical catalysis oxidative degradation ability gently The key element of weight.

The scheme shown such as CN102260003A, its numerous micro porous aeration heads being placed in reactor inner chamber bottom overflow cloth the end of at Portion, and by its alleged water distributing plate so that this micro porous aeration head overflows the effect of cloth arrangement and becomes more very, certainly, this for For using the situation of oarse-grained micron-sized photochemical catalyst of relatively easy sedimentation, really there is its favourable one side, but, From the point of view of another side, this micro porous aeration head overflows the mode that cloth arranges, and the supply of oxygen atmosphere excessively disperses, and needs most The region that need to strengthen oxygen supply is the most effective region of photochemical catalysis oxidation, due to effective in liquid water body of short wave ultraviolet Penetration depth only has 20 cm, therefore, needs most enhanced oxygen blowing real with the effective coverage promoting photochemical catalysis oxidation course It is exactly the region within quartz ampoule periphery about 20 cm distance on border, in other words, within quartz ampoule periphery about 20 cm distance Region be the region really needing the supply of enriched with oxygen atmosphere to ensure, oxygen atmosphere supply in this region is the strongest, and oxidation reaction is also Just it is proceeded more quickly；The most especially, producing electrodeless ultraviolet emission in microwave excitation mode, its feature can be accomplished greatly exactly Power, high intensity, this is the strong point of this lamp-type of electrodeless ultraviolet lamp, but, just because of its purple extraradial high power, high-strength Degree, just mates with greater need for powerful oxygen atmosphere supply capacity, and otherwise, that powerful ultraviolet radiation energy power is just Really major part is wasted.Above it is stated that, the scheme shown such as CN102260003A, factors limits Its reactor size, limits its actual treatment capacity, as its specific embodiment clearly illustrates, that Can be a single tank single treatment amount little reactor that only has about 40 liters, in the case of such little reactor, little inner chamber, Because size is the least, then, its shortcoming in terms of photochemical catalysis oxidation effective coverage oxygen supply concentration degree, would not The most obvious, it might even be possible to ignore, a problem the most non-existent can be regarded the most completely as, in the face of such Undersized little reactor, the shortcoming problem in terms of oxygen supply concentration degree, not may float mind；However, it is contemplated that Once, if described many limiting factors can be overcome, if can have that way actual implementation one is large-scale, high throughput anti- Answer device, then within above-mentioned quartz ampoule periphery 20 cm distance, effective coverage oxygen supply strengthening problem will show especially out, particularly with Using electrodeless ultraviolet lamp as the situation of UV source, within above-mentioned quartz ampoule periphery 20 cm distance, effective coverage oxygen supply is strengthened Problem is not more allowed to despise, therefore, how among the structure of possible large-scale photo-catalytical oxidation degradation reaction device, Strengthen the oxygen supply concentration degree of described effective coverage, improve the usefulness of wastewater degradation equipment, it is simply that the problem that individual needs are kept a close watch on, this is The five of problem.

The six of problem:

Within this CN102260003A scheme pumps air into the quartz ampoule including electrodeless ultraviolet lamp, reach the logical of electrodeless ultraviolet lamp Wind cooling, the purpose of cooling, and those flowings are through the air of quartz ampoule, because of by ultraviolet irradiation, some air meeting Being changed into ozone, therefore, the air flowed out from quartz ampoule is exactly the air containing some ozone certainly, and this is contained smelly by the program Oxygen air is transferred to be positioned at micro porous aeration head below reactor, and disengages from micro porous aeration head, these containing ozone bubbles from lower On ascension during, ozone contained therein can meet with the organic molecule that runs among distance and redox reaction occurs, This redox reaction can consume a part of ozone certainly, this be do not have doubt, but, above it is stated that, as The scheme that CN102260003A is shown, the many factors that cannot ignore certainly existed limit its reactor size, Limiting its actual treatment capacity, as clearly illustrating in its specific embodiment, that can only be a single tank single Treating capacity only has the little reactor of about 40 liters, in the case of such little reactor, little inner chamber, because overall dimension itself The least, then, the longitudinal size of its reactor inner chamber or regard as with reckoning in every item contain the liquid degree of depth also can only be one the least Size, clearly illustrates among this size such as its detailed description of the invention, the most about 40 centimetres, and the Sheng that reckons in every item liquid is deep Spend the most only 40 centimetres, actually contain the liquid degree of depth and be certainly less than this number, just analyze with the Sheng liquid degree of depth of 40 centimetres, that , this Sheng liquid degree of depth of 40 centimetres is what concept？That is to say, containing ozone-air ascension by the path of waste water only Having short 40 centimetre, this path is the shortest, passes through at a gallop containing ozone-air bubble and only only has 40 centimetres of deep water bodys, The shortest for time of contact with water body, contained in bubble ozone, can only have small part to be used for oxidative degradation organic matter, And most ozone actually simply passes by liquid simply, effusion emptying through exhaust port from liquid level, briefly, The oxidation potentiality major part of these ozone is wasted, and, effusion, the ozone that is wasted actually can cause need not The air pollution wanted；This case main inventive people once beat via micro porous aeration head with normal domestic use ozone machine in one meter of deep tank Enter containing ozone-air, in the case of the depth of water degree of depth reaches one meter, remain able to substantially smell the smell of ozone near the water surface, can See, that 40 centimetres of deep Sheng liquid degree of depth, it is clear that be to be not enough to fully utilized ozone；Visible, electrodeless ultraviolet light chemistry is urged For changing the such equipment of wastewater degradation reactor, ozone utilizes incomplete problem to be also required to pay close attention to, it is clear that Ren Mengeng It is contemplated that the reactor of wastewater degradation without extreme ultraviolet that ozone utilizes more completely, contaminative exhaust emissions is less, this is the six of problem.

The seven of problem:

Its running of waste water catalytic degradation reaction device, requires the expenditure of energy, and therefore, operating personnel are bound to wish, work as wastewater degradation When reaction proceeds to terminal, it is possible to impartially, the most lately immediately stop continuing to inject to inside reactor Energy；If the moment stopping Implantation Energy is too early, then wastewater degradation is incomplete；And if reaching reaction end already, the most still The most unceasingly to inside reactor Implantation Energy, that is certainly the energy in waste preciousness.As this case technical background Its structure of CN102260003A scheme can not provide any instant information to the wastewater degradation reaction end moment, then, just The terminal that wastewater degradation reacts can only be estimated by experience；And estimate, by experience, the terminal that wastewater degradation reacts, that obviously can not Satisfactory；So, how to make neither the most undelayed instant information output for the wastewater degradation reaction end moment, And immediately close the input of the energy to reactor in the just right moment, it is simply that a technical threshold that can not despise, this is The seven of problem.

The eight of problem:

Accept the described industrial wastewater of microwave and photo catalysis degradation treatment, be mingled with some the most unavoidably and originate from mechanical system abrasion process The material of metal particle and carbon granules etc, even if quantity is small, its existence is almost difficult to avoid that, the disclosure number is Described organic membrane separation assemblies in the Chinese patent application case of CN102260003A is installed in microwave and photo catalysis reaction zone, its In be installed between quartz ampoule and membrane separation assemblies certainly do not stop microwave for intercepting the dividing plate of ultraviolet, so, micro- The practical function region of ripple necessarily covers organic membrane separation assemblies institute installation area described in the program, based on membrane separation assemblies Working mechanism, its accumulation process on membrane separation assemblies organic matter top layer of the particulate of metal particle as above and carbon granules etc It is difficult to avoid that, and the particulate of this type of described metal particle and carbon granules etc, exactly the good absorption medium of microwave energy, inhale The particulate of described metal particle and the carbon granules of having received the accumulation state of microwave energy etc, its organic plasma membrane being close to can be divided by nature Produce from the top layer of assembly and based on heat penetration erosion mechanism lasting pierce destruction, be as noted previously, as this CN102260003A The structures shape of its device of application case can only select polyvinylidene fluoride film material, this polyvinylidene fluoride film material heatproof about 140 degrees Celsius, More certain than general film material heatproof high much, but, described metal particle and carbon granules of absorbing the accumulation state of microwave energy etc Its point-like of particulate pierce the heat penetration erosion effect of formula and the most easily break through the heatproof temperature limit of this polyvinylidene fluoride film material, due to above-mentioned former Cause, well imagines, the pvdf membrane material in this its device of CN102260003A application case its actual life will be the lowest In the preferable service life expected, the structure of this CN102260003A its device of application case, determine in this structural frames Under frame, above-mentioned point-like pierce formula heat penetration erosion destruction problem cannot avoid；Therefore, how to get around this point-like and pierce the heat penetration erosion of formula Destruction problem, also needs to consider, and this is the eight of problem.

The nine of problem:

The disclosure number is the Chinese patent application case of CN102260003A, the 0008th section of word of its specification disclosure text And claim Section 2, the catalyst particle size scope being suitable for for its device, there is a restriction, this particle size range limits It is that 20 nanometers are to 100 microns.It is known that some pH value be pre-adjusted not in place, pH value inappropriate in the case of, Titanium dioxide fine particles is susceptible to reunite, and then affects its effective working interface area, affects its photocatalysis usefulness；Particularly with The section of those the relatively small particle diameters among this particle size range, easily occurs because of presetting not in place, the pH value of pH value not especially The agglomeration traits appropriately caused；For this catalyst particles in the case of of reuniting, it is immediately to adopt an effective measure, enters The depolymerization of aggregate is operated by the hand-manipulating of needle；But, we, among this CN102260003A scheme, do not see any having Help immediately dissolve the structure of this problem or can immediately dissolve the scheme prompting of this problem.For such as CN102260003A scheme can only be the reactor of small scale structures because factors limits just like that, still can the most directly carry React device, carries out toppling over and inspecting outside reactor, process above-mentioned reunion situation, then, hold if likely expanding it Amount, the most so to say, if being the several cubes of large-scale reactors to dozens of cube or huge reactor, that is the most not It is manual to topple over it and operate the problem that can tackle, then, for this catalyst particles in the case of of mutually reuniting, how Realize instant disposal in situ, it is simply that a technical problem, this is the nine of problem.

The ten of problem:

The disclosure number be CN102260003A Chinese patent application case expressed by apparatus structure in, protect electrodeless purple for screen The quartz ampoule of outer lamp, its outer wall, refer to the outer wall of quartz ampoule, through for a long time with the contacting, unavoidably of processed industrial wastewater Gradually incrustation, the material that dirt amasss the most mainly is difficult to the mineral-type impurity touched by light-catalyzed reaction, because of the formation of this mechanism Incrustation phenomenon, is easy to be observed after equipment long-play；It is attached to the dirty lamination of described quartz ampoule outer wall, although The veryyest thin one layer, also be enough to cause the ultraviolet radiation of electrodeless ultraviolet lamp significantly stop, and this will cause this microwave light to be urged The actual treatment effect changing reaction treating device significantly reduces；In its reactor, the bubble of unrestrained cloth ascension is because excessively disperseing, scouring force Measuring more weak, if only relying on this more scattered bubble to maintain the bright and clean of quartz ampoule surface, really undertaking to do what is apparently beyond one's ability, in other words Saying, this more scattered bubble, what it was more weak wash away strength is still not enough to stop completely the incrustation process on this quartz ampoule surface；? During the use of laboratory yardstick, above-mentioned fouling problem is subtle, but, on commercial Application yardstick, this fouling problem Certainly will highlight；Therefore, how on the premise of not tearing machine open, immediately, effectively remove on this quartz ampoule outer wall Dirt lamination, maintains the lasting high efficiency of this microwave and photo catalysis processing means, and this problem is the most very important, and this is the ten of problem.

The 11 of problem:

Nine its problems derived of this problem problem by addressing above.Above speak of, some pH value be pre-adjusted less than In the case of position, pH value are inappropriate, titanium dioxide fine particles is susceptible to reunite, and then affects its effective working interface area, Affect its photocatalysis usefulness；Particularly with among its suitable catalyst particle size range that this CN102260003A scheme is touched upon The section of those relatively small particle diameters, easily occur especially because of pH value presetting not in place, pH value is incorrect and the group that causes Poly-problem；For this catalyst particles in the case of of reuniting, it is immediately to adopt an effective measure, carries out for aggregate Depolymerization operates；Based on this its framework of CN102260003A scheme, operating personnel cannot immediately perceive inside reactor and institute occurs State the situation of reunion, thus also cannot make instant disposal, thus, should be limited by factors and can only be small scale structures Its limited usefulness of reactor can reduce further；Therefore, among the application of reactor operates, particularly, for example, Among the application of possible large-scale reactor or huge reactor operates, the most immediately awareness inside reactor catalyst particles The main inducing parameter reunited, is a key issue, and this is the 11 of problem.

The 12 of problem:

Based on this its framework of CN102260003A scheme, due to it is stated that the restriction of factors, its reactor can only Being the smaller reactor of undersized treating capacity, the useful size of reactor inner chamber is smaller, its knot of reactor inner chamber The spatial altitude that can be used in disposing curtain type film assembly among structure is also about at 30 cm, so, even if only It is the curtain type film assembly using very small breadth, the most almost can only head on plug inside reactor in two up and down, little due to reactor Treating capacity, small size, then, after its degradation reaction completes, under the situation getting rid of liquid from inside to outside, its curtain type membrane Assembly exposes in atmosphere unavoidably, although the time every time exposed can not be grown, but, the accumulation result often bought and sold, it is simply that Make this curtain type film assembly too much with air contact, curtain type film assembly its normally use requirement, be intended under being totally submerged state Use, say, that, it is necessary to be hygrometric state use, if curtain type film assembly too much with air contact, can be made it relatively quickly Aging, Performance comparision is decayed rapidly, and this curtain type film assembly too much with the situation of air contact, at this Under its framework of CN102260003A scheme, it is impossible to avoid；Therefore, how to protect the membrane module for intercepting catalyst, make It can use in normal conditions so that it is it can be avoided that with too much the contacting of air, to safeguard its normal usage energy, really Protecting its normal service life, it is simply that the problem that needs are faced, this is the 12 of problem.

The 13 of problem:

Based on this its framework of CN102260003A scheme, among its running, the catalyst granules intercepted by curtain type film assembly, A part is at curtain type film assembly surface deposition, and another part is then trapped among liquid object phase, catalysis in thus causing liquid object mutually Agent granule density is stepped up along with the progressively reduction of liquid phase volume, and this is for follow-up UF membrane, and its UF membrane load is also Can gradually rise therewith, the problem that before and after this UF membrane load, difference is excessive needs to solve, and this is the 13 of problem.

The 14 of problem:

Based on this its framework of CN102260003A scheme, among its running, to the water pump of reactor inner chamber filling waste water, its Itself cannot differentiate inside reactor water level height, operating personnel can only rely on experience or range estimation to close this filling waste water in time Pump motor, if experience error or range estimation response are not prompt enough, it is easy to occur overflowing reactor because of waste water filling excess Situation, thereby results in unnecessary trouble；On the other hand, after degradation reaction terminates, need by inside via curtain type membrane group Part, to extracardiac pumping, is failing to know under the situation of inside reactor water level, completely can only rule of thumb or range estimation judges pass Cut off the water opportunity of pump, and so operate, hence it is evident that be unreliable, easily because of experience error or range estimation response not in time, cause this to draw water Cannot shut down in time with water pump, and this dry tap, idle running easily cause this pump motor that draws water and burns, this problem can not be neglected Depending on, this is the 14 of problem.

Summary of the invention

The technical problem to be solved is, for one of problem addressed above, two, three, four, five, six, seven, Eight, nine, ten, 11,12,13,14, and take into account collaborative, the coupling of microwave irradiation excitation and photochemical catalysis degraded Cooperation use, researches and develops a kind of novel waste water microwave and photo catalysis degradation treatment device that can solve described series of problems totally.

The present invention solves described technical problem by following scheme, and the program provides a kind of catalyst to intercept the Large Copacity light that mechanism is external Catalysis wastewater degradation device, the structure of this device includes reactor, and this reactor is the container of a hollow, and this reactor is outside it Shape profile is cube shaped, cuboid, cylindrical, the cylindroid bodily form, the polygon prism bodily form, spherical or the ellipsoid bodily form, Lower area at this reactor inner chamber is equiped with the micro porous aeration head of many, and, quartz ampoule, this quartz ampoule is erected at described The cavity position of reactor, the two ends of this quartz ampoule are equiped with closure headkerchief, lay respectively at the described closure headkerchief at quartz ampoule two ends On all offer ventilation interface, and, electrodeless ultraviolet lamp, this electrodeless ultraviolet lamp is bar-shaped, ring-type, spherical, starfish shape or sea Courage shape, the quantity of this electrodeless ultraviolet lamp is at least at more than one, and this quantity is at least all erected at more than one electrodeless ultraviolet lamp The inside of described quartz ampoule, and, air pump, this air pump is installed in the outside of reactor, and described quartz ampoule one end seal is blocked up The ventilation interface on the headkerchief wall via breather line and through reactor couples with the gas outlet of described air pump, described quartz ampoule Ventilation interface on its other end closure headkerchief exposes via another breather line and the micropore being positioned at reactor inner chamber lower area Gas head couples, and, microwave generator, this microwave generator is installed in the outside of reactor, and this microwave generator is magnetron, And, waveguide, this waveguide is the component for transmitting microwave, one end of this waveguide and described magnetron UNICOM, this ripple The other end of conduit passes through the inner chamber of the wall orientating reaction device of reactor, and, water pump, this water pump is positioned at the outside of reactor, This water pump is for pumping pending waste water, and its delivery port of this water pump leads to the inner chamber of this reactor, and this reactor is opened above to be had Exhaust port, it is important that, that one end of the wall through reactor of this waveguide extends much further into the inner chamber of reactor, And, the structure of this reactor also includes the microwave irradiation spatial domain constrainer of the caged of metal material, and the microwave irradiation of this caged is empty Being a mass of hole or the mesh of many in its structure of region constraint device, the function of the microwave irradiation spatial domain constrainer of this caged is that constraint is micro- Amplitude is according to spatial domain, and the microwave irradiation spatial domain constrainer of the caged of this metal material is exactly a metal cage, and this metal cage is installed in instead Answer the cavity position of device, this waveguide go deep into that port of reactor inner chamber and the inner chamber UNICOM of this metal cage, described UNICOM Referring to the connection in microwave channel meaning with through, described quartz ampoule is the inside being erected at this metal cage, two described ventilations Pipeline all penetrates the wall of this metal cage, and the locations of structures of the wall of this metal cage is between reactor wall and quartz ampoule outer wall Locations of structures, and, booster pump, this booster pump is mixed with the water after the degraded of a large amount of catalyst particles for supercharging pumping, should Its water inlet of the booster pump wall via ventilating water pipe and through described reactor couples with the inner chamber of described reactor, and, recoil The preposition prefilter of formula of washing, this back flush type its water inlet of preposition prefilter couples with the delivery port of described booster pump, and, Back flush type doughnut membrane microfiltration filter, described back flush type its pure water inlet of preposition prefilter is via first water purifying valve Couple with the water inlet of this back flush type doughnut membrane microfiltration filter, and, back flush type hollow-fibre membrane ultra filtration filter, Described back flush type doughnut its pure water inlet of membrane microfiltration filter is via second water purifying valve and this back flush type doughnut The water inlet of film ultra filtration filter couples, this back flush type hollow-fibre membrane its pure water inlet of ultra filtration filter and the 3rd water purifying valve Entrance point couple, the water side of the 3rd water purifying valve is the water side of outlet terminal water purification, and, catalyst underflow transition tank, This catalyst underflow transition tank is the tank body of a hollow, and this catalyst underflow transition tank deposits its backwash of described filter for temporarily The water body that catalyst concentration that program is discharged is higher, is positioned at the catalyst underflow refluxing opening of this catalyst underflow its intracavity bottom of transition tank Lead to the inner chamber of reactor via catalyst underflow return valve, this catalyst underflow return valve is for this catalyst return flow line of switch control rule Valve body, described back flush type its outlet of sewer of preposition prefilter leads to this catalyst underflow transition tank via first sewage valve Inner chamber, described back flush type doughnut its outlet of sewer of membrane microfiltration filter leads to this catalyst underflow mistake via second sewage valve Crossing the inner chamber of tank, described back flush type hollow-fibre membrane its outlet of sewer of ultra filtration filter leads to this catalyst via the 3rd sewage valve The inner chamber of underflow transition tank, each described filter is used to retain catalyst particles, and each its outlet of sewer of described filter is all converted For being subject to retain the recycling delivery outlet of catalyst particles, and, the micro porous aeration head of described many mutually assembles formation cluster-shaped Micro porous aeration head cluster, this cluster-shaped micro porous aeration head cluster is erected at the lower area of described reactor inner chamber, this group vacantly The fore-and-aft distance of tufted its bottom edge of micro porous aeration head cluster and described reactor inner chamber bottom surface between 10 centimetres with 50 centimetres it Between, this cluster-shaped micro porous aeration head cluster arround it lateral separation of edge and described reactor intracavity sidewall between 20 centimetres with Between 300 centimetres, this its center of cluster-shaped micro porous aeration head cluster or center of gravity are positioned at the underface of described quartz ampoule, and, smelly Lambda sensor, the sampling port of this its probe tube of ozone sensor is adjacent to described exhaust port or probes into described exhaust port Inside, and, ozone content display, ozone attention device or ozone content display and the composite structure of ozone attention device, be somebody's turn to do Ozone sensor warns with ozone with this ozone content display, ozone attention device or ozone content display via Article 1 cable The composite structure of device couples, and, power-supply controller of electric, its output electric signal of this ozone sensor is via Article 2 cable and this electricity Source controller couples, and this power-supply controller of electric couples with described magnetron via Article 3 cable, and this power-supply controller of electric is via Article 4 Cable couples with described air pump, and this power-supply controller of electric is can to carry out power switch action according to its described electric signal received Power-supply controller of electric, and, one group of ultrasonic transducer, this group of ultrasonic transducer at least contains a ultrasonic transducer Individuality, this group of ultrasonic transducer is used for radiating low-frequency ultrasonic waves, and this low-frequency ultrasonic waves refers to frequency at 20kHz-60kHz The ultrasonic wave of scope, this reactor inner chamber bottom surface is the most hollow to central area by periphery, described its gradient hollow between 5 degree with Between 35 degree, this group of ultrasonic transducer is that be installed in corresponding to this its hollow bosom, reactor inner chamber bottom surface with attaching The lateral surface position of partial reaction device diapire or medial surface position, and, higher-order of oscillation electric signal transmission cable, this higher-order of oscillation The one group of ultrasonic transducer in one end of electric signal transmission cable and this couples, and, higher-order of oscillation electric signal generator, described height Frequency vibration is swung the other end of electric signal transmission cable and is coupled with this higher-order of oscillation electric signal generator, and, pH pops one's head in, and, pH Analyzer, this pH probe is coupled to each other with pH analyzer, and this pH analyzer and coupling with siren, this siren is used for The pH value situation of transfiniting is sent alarm, and this pH probe stretches into reactor inner chamber through the top of reactor, and, burn through powder The micropore stainless steel sleeve that knot technique is made, this micropore stainless steel sleeve is cap for brush shape, and this micropore stainless steel sleeve is positioned at reactor Inner chamber, this micropore its blind end of stainless steel sleeve down, this its openend of micropore stainless steel sleeve upward, this micropore stainless steel sleeve Its openend upward of cylinder couples with reactor head via buffering isolating pad, and this pH pops one's head in, and it stretches into that of reactor inner chamber Within part probes into this micropore stainless steel sleeve, this its material of buffering isolating pad is fluorubber or silicon rubber, and, two to dry spring Formula ball float level controller, these two pairs of dry-reed type ball float level controllers all tops through reactor extend into the interior of reactor Chamber, a pair dry-reed type ball float level controller therein is coupled with the power cable of described water pump by a relay, therein Dry-reed type ball float level controller is coupled with the power cable of described booster pump by another by another relay, described sewage valve And described water purifying valve and described catalyst underflow return valve are all magnetic valves.

This catalyst underflow return valve is the valve body for this catalyst return flow line of switch control rule；The switch of commercially available various fluid lines Valve, may be suitable for the needs of this locations of structures, and its concrete type selecting can determine as required.

Described dry-reed type ball float level controller, the art-recognized meanings of itself for fluid level controller manufacturing professional and Speech is known；Described dry-reed type ball float level controller is commercially available.

Described relay is commercially available.

Valve body on all fluid passages of this case, can select to use magnetic valve, in the case of selecting to use magnetic valve, passes through Long-range cable is concentrated and is arranged on a control panel, so, long-distance centralized control can be conveniently realized.

Involved pH probe is commercially available；Described pH probe also known as pH sensor；PH probe or say itself skill of pH sensor Art is meant that known.

Involved pH analyzer is commercially available；Itself art-recognized meanings of pH analyzer is known.This case pH analyzer one word is general Refer to pH can be utilized to detect, picking up, showing pH value information of any model, and can externally export pH and be correlated with electric signal Instrument, market is sold simple or complicated but all meet the pH correlate meter of this basic demand it is various in style, Can select as required.

Involved buffering its thickness of isolating pad does not limits；But, have a preferred range, the preferred scope of this buffering its thickness of isolating pad Between 1 millimeter to 8 millimeter.

Themselves art-recognized meanings of involved fluorubber and involved silicon rubber is known；Involved fluorubber and involved silicon rubber, city Field is the most on sale.

Involved micropore its wall thickness of stainless steel sleeve does not limits；But, also have an associated preferred scope, this micropore stainless steel The preferred scope of its wall thickness of sleeve is between 3 millimeters to 30 millimeters.

An involved powder sintered word, the art-recognized meanings of itself, for the professional of metallurgical technology field, is known.

Involved micropore stainless steel sleeve, can customize to relevant powder metallurgy specialized factory.

The sleeve-shaped micropore stainless steel filter conversion that can be made by powder sintering process is the micropore stainless steel sleeve described in this case Cylinder；The sleeve-shaped micropore stainless steel filter that described powder sintering process is made is commercially available.

The aperture of involved micropore stainless steel its micropore of sleeve does not limits；But, the aperture of this micropore is also to have a preferred range, should The preferred scope of micropore size is between 0.5 micron to 50 micron.

This its openend upward of micropore stainless steel sleeve couples with described container top via buffering isolating pad, refers to this connection Connecing is flexible connection, in place of this connection, has described buffer compartment mediate from pad.

Described siren is can to send audio frequency warning message or the device of optical frequency warning message according to its received electric signal； Itself art-recognized meanings of described siren is known；Described siren is commercially available.

Itself art-recognized meanings of ultrasonic transducer one word is known for the professional in ultrasonic technology field.

Itself art-recognized meanings of higher-order of oscillation electric signal transmission cable one word is for the professional in ultrasonic technology field Also it is known.

Ultrasonic transducer and higher-order of oscillation electric signal transmission cable market are the most on sale；Described ultrasonic transducer and higher-order of oscillation electricity Signal transmission cables etc. also can customize to ultrasonic transducer specialized factory and cable specialized factory.

Itself art-recognized meanings of higher-order of oscillation electric signal generator one word for the professional in ultrasonic technology field also It is known；Various higher-order of oscillation electric signal generator is commercially available；Described higher-order of oscillation electric signal generator also can be to ultrasonic wave Equipment specialized factory customizes.

Involved ozone sensor is commercially available；Customize to ozone sensor specialized factory also dependent on needs.

Involved ozone content monitor market is on sale；Also dependent on needs to the customization of ozone content display specialized factory；Ozone passes Matching used ozone content display is generally also sold by sensor producer.

Involved ozone attention device, refers to warn that sound or alarm flashing or warning sound combines with alarm flashing that both are double And have for warning mechanism；Ozone attention device is commercially available；Also can be to the customization of ozone attention device specialized factory；Ozone passes Matching used ozone attention device generally also can be sold by sensor producer.

This power-supply controller of electric involved is the power-supply controller of electric that can carry out power switch action according to its described electric signal received； The power-supply controller of electric of power switch action can be carried out only with regard to its circuit engineering itself according to its electric signal received, be Through ripe, known technology；Described power-supply controller of electric is commercially available；It is possible with commercially available power-supply controller of electric to enter as required The row transformation of the way；Described power-supply controller of electric also can customize to power-supply controller of electric specialised manufacturers；The electronic device of power-supply controller of electric etc its Specialised manufacturers spreads all over the world.

Described metal material one word, the art-recognized meanings of itself, is known.

Described magnetron, and, waveguide device, waveguide, waveguide are first-class etc. expresses, and its art-recognized meanings is led for microwave technology It is known for the professional in territory.Described magnetron, and, waveguide etc., it is commercially available；Described magnetron, and, Waveguide etc., it is also possible to customize to specialized factory；Described waveguide can certainly self manufacture as required, this making for For the professional of microwave technical field, the making of waveguide device is simple.

Described quartz ampoule, its art-recognized meanings is known；Described quartz ampoule is commercially available；Described quartz ampoule also can be to specialized factory Customization.

Described electrodeless ultraviolet lamp, its art-recognized meanings is known for the professional of light sources technical field；Described electrodeless purple Outer lamp is commercially available；Its shape of described electrodeless ultraviolet lamp, size, internal filled gas, lamp wall material, lamp wall thickness, etc. Deng, it is also possible to according to specific design needs, customize to electric light source manufacturing enterprise.It is of course also possible to self manufacture.Without extreme ultraviolet Making for possessing the professional of electric light source professional knowledge of lamp, its manufacturing technology is simple.

The metal cage that metal cage described in this case can be made up of any metal material；But, in view of wastewater degradation processes involved strong Oxidative conditions, stainless steel is preferred material；The hole spread all in the metal cage self structure of this stainless steel or mesh The preferred scope of its bore is between 0.5 centimetre and 3.0 centimetres；But, if the mouth outside this scope must be selected Footpath is worth, and is also that this case is allowed.

Preferred described metal cage can be through molding, weld, rivet or assisting by screw, nut etc. by stainless steel punched-plate Property accessory splice the metal cage made.

Preferred described metal cage can also be woven, by stainless steel wire, the metal cage made.

Application this case device, waste water in reactor and by reactor inner chamber bottom bubbling on can pass through containing ozone-air Numerous holes of metal cage or mesh enter the region between metal cage and quartz ampoule, waste water with containing ozone-air in this region in the lump Participate in the photochemical catalysis oxidative degradation under microwave excitation auxiliary promotes, and by the waste water after certain degradation, again Can freely through numerous hole of metal cage or mesh by the internal outwards effusion of metal cage, the most cyclically, reciprocally, The most constantly carry out degradation, until whole waste water of whole inside reactor all reach index of degrading.

Distance between inwall and the quartz ampoule outer wall of this case metal cage does not limit, and this distance can be arbitrary distance；But, The preferred value of the distance between inwall and the outer wall of quartz ampoule of this metal cage is between 3.0 centimetres and 30.0 centimetres.

The further preferably number range of the distance between inwall and the outer wall of quartz ampoule of this metal cage is between 10.0 lis Between rice and 20.0 centimetres.

In this case device, by means of metal cage to the isolation in microwave irradiation spatial domain and restriction effect, at metal cage outer wall and reactor Region between inwall, defines microwave zero irradiation zone or the weak irradiation zone of microwave, owing to microwave basically can not affect To this region, the unhelpful dissipation of energy that microwave causes because the simple pyrogenicity of waste water absorbs in this region is contained, so, No matter how this Domain Volume expands, and is all to allow；Based on this, the structure of this case device, it is allowed to expansion is described significantly Single tank design capacity of reactor, it is allowed to expand the volume of reactor significantly, certainly, be to limit microwave by metal cage Irradiation spatial domain, and the design volume in significantly spatial domain between expanded metal cage and reactor wall realizes.Other factors, example As, microwave irradiation power, ultraviolet wavelength range, the size of ultraviolet light luminous intensity, photochemical catalyst titanic oxide nano Or the various modified catalyst nano powder used itself particle diameter, preparation technology, catalysis efficiency etc., the most all can have influence on The waste treatment capacity of this case device, these are not the emphasis of this case.

Can offer sewage draining exit in the bottom of described reactor, this sewage draining exit may be used for deslagging, removes contamination, at this Location for Sewage Can install blowoff valve, described blowoff valve is the valve controlled for blowdown.Described sewage draining exit and blowoff valve are not necessarily.

Described water pump and booster pump, be all the pump for carrying clear or turbid all kinds of water, and certainly, its pumping pressure can As desired to select arbitrarily, and, various pump market is the most on sale；This case uses different names, is intended merely to conveniently Statement, the convenient pump distinguishing each different structure position.

Described water purifying valve, sewage valve, blowoff valve, be all water valve, and various water valve market is the most on sale；About water valve, this word its The art-recognized meanings of body is known；This case uses different titles, is intended merely to conveniently state, conveniently distinguish each different structure The water valve of position.

The preferred scope in its filter opening aperture of the preposition prefilter of described back flush type is between 5 microns and 300 microns, certainly, It is also that this case is allowed that other preposition pre-filtering aperture outside this preferred scope selects；Described back flush type hollow-fibre membrane The preferred scope in its filter opening aperture of micro-filtration filter is between 25 nanometers and 1000 nanometers, certainly, this preferred scope it It is also that this case is allowed that other outer micro-filtration aperture selects；Described its filter opening aperture of back flush type hollow-fibre membrane ultra filtration filter Preferred scope be between 15 nanometers and 2 nanometers, certainly, other ultrafiltration aperture outside this scope selects also to be this Case is allowed.

The preposition prefilter of described back flush type is also referred to as back flush type fore filter or back flush type prefilter, described backwash Itself art-recognized meanings of the preposition prefilter of formula is known；The preposition prefilter of described back flush type is commercially available.

Described back flush type doughnut membrane microfiltration filter is adapted for the filter of micro-filtration；Itself technology of described micro-filtration one word It is meant that known；Itself art-recognized meanings of described back flush type doughnut membrane microfiltration filter is for technical field of membrane separation Professional for, be known；Described back flush type doughnut membrane microfiltration filter is commercially available.

Described back flush type hollow-fibre membrane ultra filtration filter is adapted for the filter of ultrafiltration；Itself technology of described ultrafiltration one word It is meant that known；Itself art-recognized meanings of described back flush type hollow-fibre membrane ultra filtration filter is for technical field of membrane separation Professional for, be known；Described back flush type hollow-fibre membrane ultra filtration filter is commercially available.

In ultrafiltration link, this back flush type hollow-fibre membrane ultra filtration filter can be that only a back flush type hollow-fibre membrane surpasses Filter the form of filter monomer；Certainly, this back flush type hollow-fibre membrane ultra filtration filter can also be at more than one by quantity Back flush type hollow-fibre membrane ultra filtration filter monomer parallel with one another couple composition.

Expressing an involved word in parallel, the art-recognized meanings itself referred to is clearly.

Express involved monomer one word, refer to itself function and structure equipment completely is individual.

Similarly, in micro-filtration link, this back flush type doughnut membrane microfiltration filter can be an only back flush type hollow The form of tunica fibrosa micro-filtration filter monomer；Certainly, this back flush type doughnut membrane microfiltration filter can also be to be existed by quantity More than one back flush type doughnut membrane microfiltration filter monomer is parallel with one another couples composition.

At described back flush type doughnut its pure water inlet of membrane microfiltration filter and described back flush type hollow-fibre membrane ultra filtration Second booster pump can be installed on the connecting pipeline of the water inlet of filter further, this second booster pump be used for augmenting hydraulic pressure with Meet the intake pressure demand of described back flush type hollow-fibre membrane ultra filtration filter；This second booster pump is not necessarily.

The structure of this case device, it is also possible to include some annexes, described annex such as: the cooling being connected with magnetron cooling pipe Water circulation system or air cooling system；Described annex the most such as being fixed on the fixed support within quartz ampoule by electrodeless ultraviolet lamp； Described annex the most such as being fixed on the support member within reactor or hanging component by described metal cage；Described annex is certain Fixed mount or the suspension bracket that described quartz ampoule is carried out within described metal cage unsettled location can also be included；Described annex is the most such as It is installed in the filter for intercepting impurity of reactor influent waste water end, etc..

It is an advantage of the invention that electrodeless ultraviolet lamp and screen thereof to be protected with metal cage shrouds in it with quartz ampoule, and metal cage retrains simultaneously The effect spatial domain of microwave, so, the spatial domain between quartz ampoule outer wall and metal cage inwall defines a microwave excitation fill-in light Chemical catalysis wastewater degradation region, and, the multiple hole of metal cage or the structure of many meshes, do not affect below waste water and reactor Bubbling and on air freely into and out of this spatial domain；And the spatial domain between metal cage and reactor wall, waste water water body is to microwave Simple pyrogenicity absorb and contained, the most significantly weaken the unhelpful dissipation of microwave energy；By significantly expanding this microwave zero spoke Design volume according to spatial domain or microwave weak irradiation spatial domain, it is possible to achieve the significantly expansion that one-pot reaction body is long-pending, it is allowed to reactor list Tank wastewater treatment capacity is substantially improved, and need not worry that microwave energy dissipates too much in unhelpful waste water water body temperature-rise effect again.

Based on this case structure, the most single tank wastewater treatment capacity of the design volume of device can be expanded to several cubes to dozens of cube； The volume of hundreds of cubes of even single tank, is also to allow；Based on this structure of this case, a complete set, whole process can be greatly reduced The frequency of operation, the beneficially saving of human and material resources.

This case, on the premise of taking into account described microwave excitation auxiliary, has been reached photocatalytic waste water degradation reactor design capacity and has significantly been expanded The target opened.

This case device its run among, its high density ascension bubble stream discharged of described cluster-shaped micro porous aeration head cluster, Upwards while ascension, and wrapped folder, carry, guided liquid-flow, form a kind of motion being similar to fountain form, this kind motion In, be derived from the high density bubble stream wrapped folder of described cluster-shaped micro porous aeration head cluster liquid gush to metal cage region and On, and then the more intensively impact inside and outside close position of metal cage, existed by described high density bubble stream wrapped folder, the liquid flow carried Impact, by the inside and outside close position of metal cage after, by the liquid layer of top area to surrounding spread, via neighboring area sink, Arrive reactor intracavity bottom region, then its high density ascension bubble stream discharged through described cluster-shaped micro porous aeration head cluster Wrapped folder, carrying, continue its motion being similar to fountain form, so circulation is endlessly；The liquid of this relatively large yardstick guided Body shuttling movement, contributes to guaranteeing the homogenization of inside reactor liquid degradation reaction process, and this urges for large-scale electrodeless ultraviolet light For changing degradation reaction device, it is necessary.

Its UV source of this case structure is to rely on microwave excited electrodeless ultraviolet lamp, and the ultraviolet radiation feature of this lamp-type is exactly permissible Accomplish high-power, high intensity, but the Effective depth penetration that ultraviolet is in liquid water body only has 20 cm, therefore, Region within quartz ampoule periphery about 20 cm distance is the effective coverage of photochemical catalysis oxidative degradation, and this region is same Time be also that microwave excitation promotes and the efficient region of photochemical catalysis oxidative degradation coupling；This effective coverage Partly or entirely it is coated with by the metal cage of also printing opacity permeable, ventilative；This case method is to be positioned at the described cluster immediately below metal cage Shape micro porous aeration head cluster, intensively discharges highdensity ascension bubble stream so that it is as fountain intensively towards as described in effectively Region discharges, and the method is favorably improved the oxygen atmosphere supply intensity of described effective coverage, helps speed up degradation reaction process.

Can significantly expand based on this case structure, the capacity of reactor or treating capacity, described significantly expand, be by significantly expanding The design volume of microwave zero irradiation zone or the weak irradiation zone of microwave realizes, then, the lateral dimension of reactor, longitudinal ruler Very little is all significantly to expand certainly, and therefore, inside reactor is contained the liquid degree of depth and can be deepened significantly similarly, such as, and can To deepen to one meter, two meters, three meters, four meters, five meters, six meters, even ten meters, etc., containing the feelings that the liquid degree of depth is the deepest Under condition, containing ozone-air bubble ascension path long enough, steep the time long enough contacted with water body, its ascension process containing ozone-air In just can be with abundant reducing substances fortune, and thoroughly or be close to and exhaust ozone contained in bubble up hill and dale, thus, Incomplete problem is utilized to be solved containing ozone composition oxidation potential in ozone-air bubble, and, due to long Ascension path cause ozone depletion, reactor tail gas re-entrainment would not have the ozone that can cause environmental pollution.

This case structure is with external multistage filter, reaches little from aggregate bulky grain to ten number nanometer to catalyst particles The interception step by step of the collision fragment of yardstick, is close to recovery, reuse photochemical catalyst up hill and dale, is close to and takes precautions against catalyst loss up hill and dale And the secondary pollution caused；This intercepts scheme step by step and secondary filter can be protected to make its filtration passage from bulky grain thing The rigid obstruction of matter；Wherein the pre-filtering aperture of the first order is between 5 microns and 300 microns, and its aperture of the micro-filtration of the second level exists Between 25 nanometers and 1000 nanometers, its aperture of the ultrafiltration of the third level is between 15 nanometers and 2 nanometers；Such interception scheme, Can fully intercept nano level photochemical catalyst, it can be close to interception gas phase this average particle of titanium dioxide P25 up hill and dale certainly Footpath is the catalyst of 21 nanometers；Address above, the gas phase titanium deoxide catalyst of nano level P25 etc, be can be a large amount of The commercially available catalyst buied, is also durability, stability, the known excellent photochemical catalyst of ultraviolet light wave band photocatalysis performance, Certainly, it is also the photochemical catalyst in fact paying the utmost attention in industrial scale applications select；This case catalyst intercepts scheme and catalyst The practical capacity of market supply, actual kind match, blend.

Further, in this case, it is external mechanism that catalyst intercepts mechanism, and based on this structure, its filter core need not be soaked in reactor The Strong oxdiative in portion, strong ultraviolet irradiation liquid in, therefore, it can need not to consider completely to ultraviolet irradiation, Strong oxdiative condition resistance to Stress, so, just without the restriction in terms of extraordinary tolerance in the selection of filter core material, can selection more vast Select in matter kind, and entirely without the material of the PVDF must being confined to again costly etc.

Involved filters at different levels are commercially available, commercially available filters at different levels, the discharge of draining-off sewage when its sewage draining exit is exactly to backwash Mouthful, this case uses this kind of back flush type equipment, is used to intercept step by step catalyst particles, the sewage draining exit of the most commercially available relevant device, The recycling delivery outlet or backflow that are used as by retaining catalyst particles by conversion in the present case use delivery outlet again.

Already described above and, can significantly expand based on this case structure, the capacity of reactor or treating capacity, described significantly expand, be Realized by the design volume significantly expanding microwave zero irradiation zone or the weak irradiation zone of microwave, then, from the appearance, The lateral dimension of reactor, longitudinal size are the most all significantly to expand, and therefore, inside reactor contains the liquid degree of depth similarly Can deepen significantly, for example, it is possible to deepen to one meter, two meters, three meters, four meters, five meters, six meters, even ten meters, etc. Deng, in the case of the Sheng liquid degree of depth is enough deep, containing ozone-air bubble ascension path long enough, the bubble containing ozone-air contacts with water body Time long enough, just can be with abundant reducing substances fortune during its ascension, and thoroughly or be close to and exhaust up hill and dale Ozone contained in bubble, thus, utilizes incomplete problem to obtain containing ozone composition oxidation potential in ozone-air bubble Thoroughly solve, and, owing to long ascension path causes ozone depletion, reactor tail gas re-entrainment would not have and can cause The ozone of environmental pollution；Only when being subject to processing reducing substances in water body i.e. organic pollution is degraded totally, in water body Through again without being available for the organic pollution of ozone oxidation reaction, those unnecessary ozone it is possible to no longer consume and pass through long Ascension path effusion liquid level；Having spoken of, among the some problem that this case solves simultaneously, is enhanced reactor The circulation of the relatively large yardstick of internal liquid, the systemic circulation mechanism that this enhances facilitates the organic dirt contained by it of inside reactor liquid The uniformity of dye thing degradation reaction process, thus, several cubes allowed in this case structure the most hundreds of to dozens of cube Under the process capacity framework of individual cube volume, when inside reactor ullage has ozone effusion, i.e. show inside reactor Degradation reaction reached terminal, and be internal liquid entirety uniformity reach the terminal of degradation reaction, this terminal point determining Factor is the matching criteria that can be provided by with this case organization plan；Ozone is installed in this case in its exhaust port position of reactor Sensor, detects ozone in this locations of structures, just means that inside reactor degradation reaction is reached home, ozone sensor And couple with the composite structure of ozone content display with ozone attention device or ozone content display or ozone attention device, be used for The information that indicates accurately, this case and the electric signal by ozone sensor output is provided to send power supply to by cable to operating personnel Controller, this power-supply controller of electric is also coupled with magnetron and air pump respectively by cable, and power-supply controller of electric is according to received by it Described electric signal carry out power switch action, certainly, its function mode is, receives ozone sensor at power-supply controller of electric and sends out When the signal of the ozone effusion sent, it is automatically switched off and leads to magnetron and the power supply of air pump；This case organization plan according to this, can and The terminal of Shi Zhixiao inside reactor degradation reaction process；And organization plan according to this, when reaction reaches terminal, it is automatically switched off magnetic Keyholed back plate and the power supply of air pump, stop to inside reactor Implantation Energy in time, so can avoid unnecessary energy waste；And And, this case structure according to this, when degradation reaction is reached home, it is possible to close described magnetron and the power supply of air pump in time, This power-off action also synchronizes, the same generation process terminating in a flash ozone, owing to ozone generation process is terminated in time, The a large amount of ozone that would not have more than needs disengage from described exhaust port, thus avoid unnecessary secondary pollution or say secondary Raw pollution；Its framework of this case determines the ozone that it does not have more than needed and is available for discharge.

Among this case structure, the microwave irradiation spatial domain of its inside reactor is cut off by forcing, limits, this case and use external Cascading multiple stages backwash filter structure intercepts catalyst particles, back flush type hollow fiber microfiltration membrane assembly therein subtly And back flush type polysulfone hollow fiber ultrafiltration membrane system is the most external and away from reactor core, microwave can not be irradiated to described film group completely Part, based on this structure of this case, has got around described point-like completely and has pierced the heat penetration erosion destruction problem of formula, and this problem thus obtains well Solution.

This case reactor inner chamber bottom surface is the most hollow to central area by periphery, described its gradient hollow between 5 degree with 35 degree it Between, this case ultrasonic transducer is to be installed in its part reaction corresponding to hollow bosom of this reactor inner chamber bottom surface with attaching The lateral surface position of device diapire or medial surface position；Addressing above, this case structure and beneficially driving a reaction device internal liquid make phase Shuttling movement to large scale, the mode of this liquid shuttling movement is that peripheral liquid sinks, and middle liquid rises, the most constantly Move in circles；Address above, some pH value be pre-adjusted not in place, pH value inappropriate in the case of, titanium dioxide is micro- Grain is susceptible to reunite, and then affects its effective working interface area, affects its photocatalysis usefulness；Particularly with this particle size range Among the section of those relatively small particle diameters, easily occur especially because of pH value presetting not in place, pH value is incorrect and cause Agglomeration traits；For this catalyst particles in the case of of reuniting, it is immediately to adopt an effective measure, carries out for aggregate Depolymerization running；When catalyst particles generation serious agglomeration, the heavier macro aggregate of some of which is due to gravity Effect, it is intended to gradually settling to reactor intracavity bottom, in this case structure, reactor intracavity bottom is hollow structure, and, This case structure can make the shuttling movement of described relatively large yardstick by driving a reaction device internal liquid, the effect of this systemic circulation campaign together with The effect of ubiquitous natural gravity, the macro aggregate settled can be pushed away along the slope of described hollow structure sweep to hollow Depths also makes them be gathered in there, and in this case structure, ultrasonic transducer is just being in this hollow innermost locations of structures, should Hollow innermost region, is the region finally assembled of described macro aggregate, be also simultaneously ultrasonic wave can minimum damply, Minimum distance ground, carry out depolymerization operating area the most consumingly, most effectively for macro aggregate；This structure of this case can allow for Minimum ultrasonic energy loss, it is achieved maximized ultrasonic depolymerization effect；This case structure according to this, it is possible to converge aggregate precipitum, And the region concentrated most at aggregate precipitum, implement depolymerization running；The ultrasonic wave being derived from reactor bottom also is able to of course simultaneously Other region being radiated in inside reactor liquid, plays the aggregate being still within suspended state that those are smaller and solves Poly-effect；This case associated ultrasonic radiates mechanism, is the mechanism that can start as required or close；This case thus achieve for The instant of this catalyst particles agglomeration traits is disposed in situ.

Structure is protected for screen the quartz ampoule of electrodeless ultraviolet lamp, its outer wall, refers to the outer wall of quartz ampoule, through long and quilt Processing the contact of industrial wastewater, the most gradually incrustation, the material that dirt amasss the most mainly is difficult to the nothing touched by light-catalyzed reaction Machine class impurity, the incrustation phenomenon formed because of this mechanism, it is easy to be observed after equipment long-play；It is attached to described The dirty lamination of quartz ampoule outer wall, although the veryyest thin one layer, also be enough to cause the ultraviolet radiation of electrodeless ultraviolet lamp significantly Stopping, the actual treatment effect causing this microwave and photo catalysis reaction treating device is significantly reduced by this；This case structure is positioned at reaction Ultrasonic transducer bottom device, in the irregular depolymerization running carried out for accidental catalyst particles serious agglomeration situation Among, its ultrasonic wave radiated, the most also can arrive quartz ampoule place locations of structures, this ultrasonic wave is carrying out depolymerization fortune in situ While work, carry out amassing for quartz ampoule surface dirt the ultrasonic clean scale removal work of thing the most in the lump；Further, ultrasonic transducer Installation position away from quartz ampoule place locations of structures, ultrasonic radiation has decayed when arriving quartz ampoule position, therefore, stone Ultrasonic impact suffered by English tube-surface is low intensive ultrasonic impact, and this low intensive ultrasonic impact can leniently remove Dirt, is avoided that again or significantly weakens its quartz ampoule surface smoothness loss being likely to result in of ultrasonic cavitation；Should based on this case Structure, it is possible on the premise of not tearing machine open, removes the dirty lamination on this quartz ampoule outer wall immediately, effectively, thereby safeguards that this is micro- The lasting high efficiency of glistening light of waves catalytic degradation reaction device.

The pH value of wastewater degradation inside reactor water body, is the key factor affecting catalyst dispersion stabilization；This case structure fills If pH probe and the pH value display instrument of association and the siren etc. that is associated, it is possible to steady beyond catalyst dispersion in pH value In the case of determining scope, actively sending alarm, based on this structure of this case, associative operation personnel can the inside reactor of awareness immediately Agglomeration is inclined to, and makes instant disposal.Described micropore stainless steel sleeve in this case structure and installing mode thereof, be and this The indispensable important component that case principle and this case structure match.

Membrane module in this case structure, is to be in all the time to be totally submerged among the operating mode of use, and membrane module therein has no chance to connect Touch air, be always maintained at hygrometric state and the state being totally submerged, therefore, there will be no the film group easily occurred in that background technology Part is often exposed to the situation in air, and its applying working condition of the membrane module in this case structure more conforms to membrane module, and itself is intrinsic Use condition requirement, is more conducive to safeguard its normal usage energy of membrane module, is more conducive to guarantee its normal service life of membrane module.

This case structure arranges catalyst underflow transition tank, for temporarily depositing from each its backwashing procedures of back flush type filter The liquid that the concentration containing catalyst washed away is higher, thus avoid liquid higher for this catalyst concentration is directly filled back reaction Device, so, it is to avoid the problem that in inside reactor liquid, catalyst concentration is stepped up along with the extraction process of water purification, this can Extract with the water purification follow-up to it and reduce the heavy burdens, had so one catalyst underflow transition tank structure, it is possible to extract journey at water purification After sequence completes, then within catalyst underflow is filled back reactor.

The dry-reed type ball float liquid that in this case structure a pair couples with its power cable of water pump of described transport wastewater through relay Level controller, its exist, it is possible to automatically avoid excess filling waste water to reactor inner chamber, and thus avoid waste water overflow reactor； Another dry-reed type ball float level controller to coupling with its power cable of described booster pump through another relay, its existence, It can be avoided that the liquid of inside reactor is excessively extracted and causes the idle running of this booster pump, dry turns, booster motor so can be avoided Burn.

Described sewage valve in this case structure and described water purifying valve and described catalyst underflow return valve are all magnetic valves, can be by These magnetic valve relevant cables are concentrated and are arranged to a panel, and this structure allows the valve body corresponding to each program of long-distance centralized control Switch motion.

In short, this case utilizes metal cage to retrain microwave more closely, reach and allowed reactor design capacity significantly to expand Target；Meanwhile, its scheme also enhances the shuttling movement of relatively large yardstick of inside reactor liquid；The program to be set up in Its highdensity bubble stream discharged of described cluster-shaped micro porous aeration head cluster immediately below metal cage, it is achieved degrade for emphasis Being substantially improved of the oxygen supply concentration degree of reaction zone；The program and having reached for nm-class catalyst particulate from big of its aggregate Grain to ten number nanometers collision fragments widely, fine interception；Based on this organization plan, the selection face of its filter core material is also Thus expanded；Its degradation reaction endpoint information can be known in time；It is right to be automatically switched off when its degradation reaction terminal The energy input of reactor；When its degradation reaction terminal, terminate the generation process of ozone the most in time, it is to avoid need not The secondary pollution wanted；Its structure also can dispose accidental catalyst particles serious agglomeration situation the most in situ, the most incidentally Quartz ampoule surface described in the supersonic cleaning of the low intensive gentleness after weakening through teletransmission appropriateness, keeps it excellent Ultraviolet light transparent performance；Its structure also can actively detect agglomeration tendency, and send alarm when relevant parameter exceeds standard；Its knot Structure beneficially membrane module are being totally submerged use among operating mode；Its structure and realize catalyst by catalyst underflow transition tank structure The appropriate transition of underflow is deposited, and overcomes the problem that difference before and after UF membrane load is excessive；Its structure and be capable of waste water Automatically controlling of perfusion water level；Its structure also can close described increasing when water purification extraction to restricted water supply position automatically, in time The protection of the power supply of press pump, beneficially booster motor.

This case solves described series of problems totally.

Accompanying drawing explanation

Fig. 1 is the brief perspective diagram of this case apparatus structure.

In figure, 1 is reactor, and 2 is the microwave irradiation spatial domain constrainer of caged, and it is exactly a metal cage, and 3 is quartz ampoule, 4 is electrodeless ultraviolet lamp, and 5,12 is two closure headkerchieves of quartz ampoule respectively, and 6 is exhaust port, and 7 is waveguide, and 8 are Magnetron, 9 is air pump, and 10,14 is the breather line that two-strip structure position is different respectively, and 11 indicate reactor contains liquid operation The rough position of waste water liquid level time inside, 13 is microwave zero irradiation zone or micro-between metal cage outer wall and reactor wall The weak irradiation zone of ripple, 15 is micro porous aeration head, and 16 is blowoff valve, and 17 is sewage draining exit, and 18 is that back flush type hollow-fibre membrane surpasses Filtering filter, 19 is back flush type doughnut membrane microfiltration filter, and 20 is the preposition prefilter of back flush type, and 21 is supercharging Pump, 22 is water pump, and 23 is the probe tube of ozone sensor, and 24 is ozone content display, ozone attention device or ozone content Display and the composite structure of ozone attention device, 25 is ozone sensor, and 26 is power-supply controller of electric, and 27 is ultrasonic transducer, 28 is higher-order of oscillation electric signal transmission cable, and 29 is siren, and 30 is cable pH analyzer and siren linked up, 31 is pH analyzer, and 32 is the cable linked up of pH analyzer and pH being popped one's head in, and 33 is pH probe, 34 be micropore not Rust steel bushing, 35 is catalyst underflow transition tank, and 36 is catalyst underflow return valve, and the some arrows in figure indicate it adjacent to pipeline Liquid flow direction when in an ON state.

Detailed description of the invention

In this case embodiment that Fig. 1 is shown, the structure of this example device includes reactor 1, and this reactor 1 is a hollow Container, this its appearance profile of reactor 1 is cube shaped, cuboid, cylindrical, the cylindroid bodily form, multiedge cylinder Shape, spherical or the ellipsoid bodily form, the lower area at this reactor 1 inner chamber is equiped with the micro porous aeration head 15 of many, mark 15 is only to indicate micro porous aeration head individuality, and 15 only indicate the individual morphology of micro porous aeration head, and, quartz ampoule 3, this stone English pipe 3 is erected at the cavity position of described reactor, and the two ends of this quartz ampoule 3 are equiped with closure headkerchief 5,12, lay respectively at Ventilation interface is all offered on the described closure headkerchief 5,12 at quartz ampoule 3 two ends, and, electrodeless ultraviolet lamp 4, this electrodeless purple Outer lamp 4 is in bar-shaped, ring-type, spherical, starfish shape or sea urchin shape, and the quantity of this electrodeless ultraviolet lamp 4, should at least at more than one Quantity is at least all erected at the inside of described quartz ampoule 3 at more than one electrodeless ultraviolet lamp 4, and, air pump 9, this sky Air pump 9 is installed in the outside of reactor 1, and the ventilation interface on described quartz ampoule 3 one end seal blanking cover head 5 is via breather line 10 and couple with the gas outlet of described air pump 9 through the wall of reactor 1, described its other end of quartz ampoule 3 blocks headkerchief 12 On ventilation interface couple with the micro porous aeration head 15 being positioned at reactor 1 inner chamber lower area via another breather line 14, And, microwave generator, this microwave generator is installed in the outside of reactor 1, and this microwave generator is magnetron 8, and, Waveguide 7, this waveguide 7 is the component for transmitting microwave, one end of this waveguide 7 and described magnetron 8 UNICOM, should The other end of waveguide 7 passes through the inner chamber of the wall orientating reaction device 1 of reactor 1, and, water pump 22, this water pump 22 is positioned at The outside of reactor 1, this water pump 22 is for pumping pending waste water, and this its delivery port of water pump 22 leads to this reactor 1 Inner chamber, this reactor 1 is opened above exhaust port 6, it is important that, that of the wall through reactor 1 of this waveguide 7 One end extends much further into the inner chamber of reactor 1, and, the structure of this reactor 1 also includes the micro-of the caged of metal material Amplitude, according to spatial domain constrainer 2, is a mass of hole or the mesh of many in its structure of microwave irradiation spatial domain constrainer 2 of this caged, The function of the microwave irradiation spatial domain constrainer 2 of this caged is constraint microwave irradiation spatial domain, the microwave irradiation of the caged of this metal material Spatial domain constrainer 2 is exactly a metal cage, and this metal cage 2 is installed in the cavity position of reactor 1, going deep into of this waveguide 7 That port of reactor 1 inner chamber and the inner chamber UNICOM of this metal cage 2, described UNICOM refers to the connection in microwave channel meaning With through, described quartz ampoule 3 is the inside being erected at this metal cage 2, and two described breather lines 10,14 all penetrate this gold Belonging to the wall of cage 2, the locations of structures of the wall of this metal cage 2 is the structure position between reactor 1 inwall and quartz ampoule 3 outer wall Put, and, booster pump 21, this booster pump 21 is mixed with the water after the degraded of a large amount of catalyst particles for supercharging pumping, should Its water inlet of booster pump 21 wall via ventilating water pipe and through described reactor 1 couples with the inner chamber of described reactor 1, with And, the preposition prefilter of back flush type 20, its water inlet of the preposition prefilter of this back flush type 20 goes out with described booster pump 21 The mouth of a river couples, and, back flush type doughnut membrane microfiltration filter 19, it is clean for the preposition prefilter of described back flush type 20 Water out couples via the water inlet of first water purifying valve with this back flush type doughnut membrane microfiltration filter 19, and, instead Flushing type hollow-fibre membrane ultra filtration filter 18, described back flush type its pure water inlet of doughnut membrane microfiltration filter 19 via Second water purifying valve couples with the water inlet of this back flush type hollow-fibre membrane ultra filtration filter 18, this back flush type doughnut The entrance point of its pure water inlet of film ultra filtration filter 18 and the 3rd water purifying valve couples, and the water side of the 3rd water purifying valve is defeated Go out the water side of terminal water purification, and, catalyst underflow transition tank 35, this catalyst underflow transition tank 35 is the tank body of a hollow, This catalyst underflow transition tank 35 deposits the catalyst concentration that described its backwashing procedures of filter 18,19,20 is discharged for temporarily The highest water body, the catalyst underflow refluxing opening being positioned at this catalyst its intracavity bottom of underflow transition tank 35 refluxes via catalyst underflow Valve 36 leads to the inner chamber of reactor 1, and this catalyst underflow return valve 36 is the valve body for this catalyst return flow line of switch control rule, Its outlet of sewer of the preposition prefilter of described back flush type 20 is via first sewage valve and towards this catalyst underflow transition tank 35 Inner chamber, it is dense that described back flush type its outlet of sewer of doughnut membrane microfiltration filter 19 leads to this catalyst via second sewage valve The inner chamber of slurry transition tank 35, described back flush type its outlet of sewer of hollow-fibre membrane ultra filtration filter 18 is via the 3rd sewage valve Towards the inner chamber of this catalyst underflow transition tank 35, each described filter is used to retain catalyst particles, each described filter 20, 19,18 its outlets of sewer are all converted as by retaining the recycling delivery outlet of catalyst particles, and, the micropore of described many exposes Gas head 15 mutually assembles formation cluster-shaped micro porous aeration head cluster, and this cluster-shaped micro porous aeration head cluster is erected at described vacantly The lower area of reactor 1 inner chamber, this cluster-shaped its bottom edge of micro porous aeration head cluster and described reactor 1 inner chamber bottom surface Fore-and-aft distance is between 10 centimetres and 50 centimetres, and the arbitrarily selected value within the scope of this fore-and-aft distance is all available enforcement value, Such as this fore-and-aft distance can be 10 centimetres, 20 centimetres, 30 centimetres, 40 centimetres, 50 centimetres, etc., this cluster-shaped is micro- Hole aeration head cluster arround it lateral separation of edge and described reactor intracavity sidewall between 20 centimetres and 300 centimetres, Arbitrarily selected value within the scope of this lateral separation be all available enforcement value, such as this lateral separation can be 20 centimetres, 60 Centimetre, 100 centimetres, 160 centimetres, 250 centimetres, 300 centimetres, etc., this its center of cluster-shaped micro porous aeration head cluster or Center of gravity is positioned at the underface of described quartz ampoule, and, ozone sensor 25, the sampling of this its probe tube 23 of ozone sensor 25 Port adjacent to described exhaust port 6 or the inside that probes into described exhaust port 6, and, ozone content display, ozone The composite structure 24 of attention device or ozone content display and ozone attention device, this ozone sensor 25 via Article 1 cable with This ozone content display, ozone attention device or ozone content display couple with the composite structure 24 of ozone attention device, and, Power-supply controller of electric 26, this its output electric signal of ozone sensor 25 couples with this power-supply controller of electric 26 via Article 2 cable, should Power-supply controller of electric 26 couples with described magnetron 8 via Article 3 cable, and this power-supply controller of electric 26 is via Article 4 cable and institute Stating air pump 9 to couple, this power-supply controller of electric 26 is can to carry out power switch action according to its described electric signal received Power-supply controller of electric, and, one group of ultrasonic transducer 27, this group of ultrasonic transducer 27 at least contains a ultrasonic waves Energy device is individual, and this group of ultrasonic transducer 27 is used for radiating low-frequency ultrasonic waves, and this low-frequency ultrasonic waves refers to frequency at 20kHz The ultrasonic wave of-60kHz scope, this reactor 1 inner chamber bottom surface is the most hollow to central area by periphery, described its gradient hollow Between 5 degree and 35 degree, this group of ultrasonic transducer 27 is to be installed in this reactor 1 inner chamber bottom surface it is hollow with attaching The lateral surface position of the part reactor diapire corresponding to bosom or medial surface position, what meaning ground shown in legend was shown is dress It is located at the situation of lateral surface position, legend does not has to show the situation being installed in medial surface position, and, higher-order of oscillation electric signal Transmission cable 28, the one group of ultrasonic transducer 27 in one end of this higher-order of oscillation electric signal transmission cable 28 and this couples, and, Higher-order of oscillation electric signal generator, the other end of described higher-order of oscillation electric signal transmission cable 28 is sent out with this higher-order of oscillation electric signal Raw device couples, and, pH probe 33, and, pH analyzer 31, this pH probe 33 is coupled to each other with pH analyzer 31, This pH analyzer 31 and coupling with siren 29, this siren 29 for the pH value situation of transfiniting is sent alarm, this pH Probe 33 stretches into reactor 1 inner chamber through the top of reactor 1, and, through the micropore stainless steel that powder sintering process is made Sleeve 34, this micropore stainless steel sleeve 34 is in cap for brush shape, and this micropore stainless steel sleeve 34 is positioned at reactor 1 inner chamber, this micropore Its blind end of stainless steel sleeve 34 down, this its openend of micropore stainless steel sleeve 34 upward, this micropore stainless steel sleeve 34 Its openend upward, via buffering isolating pad and reactor 1 top attachment, is depicted without that described buffering isolation in legend Pad, within this pH probe 33 its those parts stretching into reactor 1 inner chamber probe into this micropore stainless steel sleeve 34, this buffering Its material of isolating pad is fluorubber or silicon rubber, and, two pairs of dry-reed type ball float level controllers, these two pairs of dry-reed type ball float liquid Level controller all tops through reactor 1 extend into the inner chamber of reactor 1, a pair dry-reed type ball float level controller therein Being coupled by the power cable of a relay with described water pump 22, dry-reed type ball float level controller is passed through by therein another Another relay couples with the power cable of described booster pump 21, described sewage valve and described water purifying valve and described catalyst Underflow return valve is all magnetic valve.

Involved magnetic valve is commercially available.

This catalyst underflow return valve is the valve body for this catalyst return flow line of switch control rule；The switch of commercially available various fluid lines Valve, may be suitable for the needs of this locations of structures, and its concrete type selecting can determine as required.

Described dry-reed type ball float level controller, the art-recognized meanings of itself for fluid level controller manufacturing professional and Speech is known；Described dry-reed type ball float level controller is commercially available.

Described relay is commercially available.

Valve body on all fluid passages of this case, can select to use magnetic valve, in the case of selecting to use magnetic valve, passes through Long-range cable is concentrated and is arranged on a control panel, so, long-distance centralized control can be conveniently realized.

Legend is depicted without described dry-reed type ball float level controller.

Legend is depicted without this higher-order of oscillation electric signal generator and another higher-order of oscillation electric signal generator described.

Involved pH probe is commercially available；Described pH probe also known as pH sensor；PH probe or say itself skill of pH sensor Art is meant that known.

Involved pH analyzer is commercially available；Itself art-recognized meanings of pH analyzer is known.This case pH analyzer one word is general Refer to pH can be utilized to detect, picking up, showing pH value information of any model, and can externally export pH and be correlated with electric signal Instrument, market is sold simple or complicated but all meet the pH correlate meter of this basic demand it is various in style, Can select as required.

Involved buffering its thickness of isolating pad does not limits；But, have a preferred range, the preferred scope of this buffering its thickness of isolating pad Between 1 millimeter to 8 millimeter.

Themselves art-recognized meanings of involved fluorubber and involved silicon rubber is known；Involved fluorubber and involved silicon rubber, city Field is the most on sale.

Involved micropore its wall thickness of stainless steel sleeve does not limits；But, also have an associated preferred scope, this micropore stainless steel The preferred scope of its wall thickness of sleeve is between 3 millimeters to 30 millimeters.

An involved powder sintered word, the art-recognized meanings of itself, for the professional of metallurgical technology field, is known.

Involved micropore stainless steel sleeve, can customize to relevant powder metallurgy specialized factory.

The sleeve-shaped micropore stainless steel filter conversion that can be made by powder sintering process is the micropore stainless steel sleeve described in this case Cylinder；The sleeve-shaped micropore stainless steel filter that described powder sintering process is made is commercially available.

The aperture of involved micropore stainless steel its micropore of sleeve does not limits；But, the aperture of this micropore is also to have a preferred range, should The preferred scope of micropore size is between 0.5 micron to 50 micron.

This its openend upward of micropore stainless steel sleeve couples with described container top via buffering isolating pad, refers to this connection Connecing is flexible connection, in place of this connection, has described buffer compartment mediate from pad.

Described siren is can to send audio frequency warning message or the device of optical frequency warning message according to its received electric signal； Itself art-recognized meanings of described siren is known；Described siren is commercially available.

Described its gradient enforcement value hollow is between 5 degree and 35 degree, and the arbitrarily selected value within this range of grade is all this The enforcement value that can use that case allows；This its gradient enforcement value hollow can be such as 5 degree, 8 degree, 10 degree, 15 degree, 20 Degree, 25 degree, 30 degree, 35 degree, etc..

Itself art-recognized meanings of involved ultrasonic transducer one word is known for the professional in ultrasonic technology field 's.

Itself art-recognized meanings of involved higher-order of oscillation electric signal transmission cable one word is for the professional in ultrasonic technology field For be also known.

Involved ultrasonic transducer and higher-order of oscillation electric signal transmission cable market are the most on sale；Described ultrasonic transducer and high frequency vibrating Swing electric signal transmission cable etc. also to customize to ultrasonic transducer specialized factory and cable specialized factory.

Involved higher-order of oscillation electric signal generator one word itself art-recognized meanings for ultrasonic technology field professional and Speech is also known；Various higher-order of oscillation electric signal generator is commercially available；Described higher-order of oscillation electric signal generator also can be to super The customization of sound wave equipment specialized factory.

Involved ozone sensor 25 is commercially available；Customize to ozone sensor specialized factory also dependent on needs.

Involved ozone content monitor market is on sale；Also dependent on needs to the customization of ozone content display specialized factory；Ozone passes Matching used ozone content display is generally also sold by sensor producer.

Involved ozone attention device, refers to warn that sound or alarm flashing or warning sound combines with alarm flashing that both are double And have for warning mechanism；Ozone attention device is commercially available；Also can be to the customization of ozone attention device specialized factory；Ozone passes Matching used ozone attention device generally also can be sold by sensor producer.

This power-supply controller of electric 26 involved is the power supply control that can carry out power switch action according to its described electric signal received Device；The power-supply controller of electric of power switch action can be carried out only with regard to its circuit engineering itself according to its electric signal received, It it is ripe, known technology；Described power-supply controller of electric is commercially available；It is possible with commercially available power-supply controller of electric according to need Change a social system；Described power-supply controller of electric also can customize to power-supply controller of electric specialised manufacturers；The electronics device of power-supply controller of electric etc Its specialised manufacturers of part spreads all over the world.

Described metal material one word, the art-recognized meanings of itself, is known.

The metal cage that metal cage 2 can be made up of any metal material；But, in view of wastewater degradation processes involved strong oxidizing property Condition, stainless steel is preferred material.

The hole spread all in this metal cage 2 self structure or the preferred scope of its bore of mesh be between 0.5 centimetre with 3.0 centimetres it Between, the arbitrarily selected value within the scope of this is preferred is all the most available enforcement value, and such as, its bore value can be 0.5 Centimetre, 1.0 centimetres, 1.75 centimetres, 2.0 centimetres, 3.0 centimetres, etc.；If must select to use this preferred scope Outside bore value, that is also that this case is allowed.

Preferred described metal cage 2 can be through molding, weld, rivet or being auxiliary by screw, nut etc. by stainless steel punched-plate Helping property accessory splices the metal cage made.

Preferred described metal cage 2 can also be woven, by stainless steel wire, the metal cage made.

Distance between inwall and quartz ampoule 3 outer wall of metal cage 2 does not limit, and this distance can be arbitrary distance；But, The preferred value of the distance between inwall and the outer wall of quartz ampoule 3 of this metal cage 2 is between 3.0 centimetres and 30.0 centimetres, Any numerical value within the scope of this is all the preferred value allowing to implement, such as, the numerical value of this distance can be 3.0 centimetres, 8.0 centimetres, 16.5 centimetres, 22 centimetres, 30 centimetres, etc..

The further preferably number range of the distance between inwall and the outer wall of quartz ampoule 3 of metal cage 2 is between 10.0 lis Between rice and 20.0 centimetres, any numerical value within the scope of this is all the further preferably numerical value allowing to implement, and such as should Distance value can be 10 centimetres, 15 centimetres, 18 centimetres, 20 centimetres, etc..

Can offer sewage draining exit 17 in the bottom of described reactor 1, this sewage draining exit 17 may be used for deslagging, removes contamination, this row Blowoff valve 16 can be installed in dirty mouth 17 position, and described blowoff valve 16 is the valve controlled for blowdown.Described sewage draining exit 17 with And blowoff valve 16 is not necessarily.

Described water pump 22 and booster pump 21, be all the pump for carrying clear or turbid all kinds of water, certainly, its pumping pressure Can as desired to select arbitrarily, and, various pump market is the most on sale；This case uses different names, is simply Facilitate statement, the convenient pump distinguishing each different structure position.

Described water purifying valve, sewage valve, blowoff valve, be all water valve, and various water valve market is the most on sale；About water valve, this word its The art-recognized meanings of body is known；This case uses different titles, is intended merely to conveniently state, conveniently distinguish each different structure The water valve of position.

The preferred scope in its filter opening aperture of the preposition prefilter of described back flush type 20 is between 5 microns and 300 microns, Arbitrarily selected value within the scope of this is all the most available enforcement value, and certainly, other outside this preferred scope is preposition It is also that this case is allowed that pre-filtering aperture selects；Described its filter opening aperture of back flush type doughnut membrane microfiltration filter 19 Preferably scope is between 25 nanometers and 1000 nanometers, and the arbitrarily selected value within the scope of this is preferred is all the most available Enforcement value, certainly, it is also that this case is allowed that other micro-filtration aperture outside this preferred scope selects；Described back flush type The preferred scope in its filter opening aperture of hollow-fibre membrane ultra filtration filter 18 is between 15 nanometers and 2 nanometers, this preferred model Arbitrarily selected value within enclosing is all the most available enforcement value, and certainly, other ultrafiltration aperture outside this scope selects also It is that this case is allowed.

The preposition prefilter of described back flush type 20 also referred to as back flush type fore filter or back flush type prefilter, described instead Itself art-recognized meanings of the preposition prefilter of flushing type 20 is known；Described back flush type preposition prefilter 20 market has Sell.

Described back flush type doughnut membrane microfiltration filter 19 is adapted for the filter of micro-filtration；Described micro-filtration one word itself Art-recognized meanings is known；Itself art-recognized meanings of described back flush type doughnut membrane microfiltration filter 19 is for UF membrane For the professional of technical field, it is known；Described back flush type doughnut membrane microfiltration filter 19 is commercially available.

Described back flush type hollow-fibre membrane ultra filtration filter 18 is adapted for the filter of ultrafiltration；Described ultrafiltration one word itself Art-recognized meanings is known；Itself art-recognized meanings of described back flush type hollow-fibre membrane ultra filtration filter 18 is for UF membrane For the professional of technical field, it is known；Described back flush type hollow-fibre membrane ultra filtration filter 18 is commercially available.

In ultrafiltration link, this back flush type hollow-fibre membrane ultra filtration filter 18 can be an only back flush type doughnut The form of film ultra filtration filter monomer；Certainly, this back flush type hollow-fibre membrane ultra filtration filter can also be at one by quantity Above back flush type hollow-fibre membrane ultra filtration filter monomer is parallel with one another couples composition.

Expressing an involved word in parallel, the art-recognized meanings itself referred to is clearly.

Express involved monomer one word, refer to itself function and structure equipment completely is individual.

Similarly, in micro-filtration link, this back flush type doughnut membrane microfiltration filter 19 can be an only back flush type The form of doughnut membrane microfiltration filter monomer；Certainly, this back flush type doughnut membrane microfiltration filter can also be by counting Measure and form in more than one back flush type doughnut membrane microfiltration filter monomer parallel with one another connection.

In described back flush type its pure water inlet of doughnut membrane microfiltration filter 19 and described back flush type hollow-fibre membrane ultrafiltration Can install second booster pump on the connecting pipeline of the water inlet of filter 18 further, this second booster pump is used for augmenting Hydraulic pressure is to meet the intake pressure demand of described back flush type hollow-fibre membrane ultra filtration filter；This second booster pump is not necessary to 's.

This case its structure of device embodiment, it is also possible to include some annexes, described annex such as: with magnetron 8 cooling pipe even The cooling water recirculation system connect or air cooling system；Described annex is the most such as within being fixed on quartz ampoule 3 by electrodeless ultraviolet lamp 4 Fixed support；Described annex the most such as being fixed on the support member within reactor 1 or hanging component by described metal cage； Described annex can certainly include within described metal cage 2, described quartz ampoule 3 being carried out the fixed mount of unsettled location or hanging Frame；Described annex is the most such as the bracing frame of unsettled location described cluster-shaped micro porous aeration head cluster or fixed mount or suspension bracket；Institute State annex and be the most such as installed in the filter for intercepting impurity of reactor 1 influent waste water end, etc..

Implement legend is depicted without described annex.

The embodiment of this case is not limited to legend mode.

Claims (10)

1. catalyst intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external, and the structure of this device includes reactor, this reactor The container of a hollow, its appearance profile of this reactor be cube shaped, cuboid, cylindrical, the cylindroid bodily form, The polygon prism bodily form, spherical or the ellipsoid bodily form, the lower area at this reactor inner chamber is equiped with the micro porous aeration head of many, with And, quartz ampoule, this quartz ampoule is erected at the cavity position of described reactor, and the two ends of this quartz ampoule are equiped with closure headkerchief, point It is not positioned on the described closure headkerchief at quartz ampoule two ends and all offers ventilation interface, and, electrodeless ultraviolet lamp, this electrodeless ultraviolet lamp In bar-shaped, ring-type, spherical, starfish shape or sea urchin shape, the quantity of this electrodeless ultraviolet lamp is at least one, and this quantity is at least one Individual electrodeless ultraviolet lamp is erected at the inside of described quartz ampoule, and, air pump, this air pump is installed in the outside of reactor, Ventilation interface on described quartz ampoule one end seal blanking cover head is via breather line and through the wall of reactor and described air pump Gas outlet couple, its other end of described quartz ampoule closure headkerchief on ventilation interface via another breather line be positioned at reactor The micro porous aeration head of inner chamber lower area couples, and, microwave generator, this microwave generator is installed in the outside of reactor, This microwave generator is magnetron, and, waveguide, this waveguide is the component for transmitting microwave, one end of this waveguide With described magnetron UNICOM, the other end of this waveguide passes through the inner chamber of the wall orientating reaction device of reactor, and, water pump, should Water pump is positioned at the outside of reactor, and this water pump is for pumping pending waste water, and its delivery port of this water pump leads to the interior of this reactor Chamber, this reactor is opened above exhaust port, it is characterised in that one end of the wall through reactor of this waveguide is entered One step extends into the inner chamber of reactor, and, the structure of this reactor also includes the microwave irradiation spatial domain of the caged of metal material Constrainer, is a mass of hole or mesh, the microwave spoke of this caged of many in microwave irradiation spatial domain its structure of constrainer of this caged Function according to spatial domain constrainer is constraint microwave irradiation spatial domain, and the microwave irradiation spatial domain constrainer of the caged of this metal material is exactly one Individual metal cage, this metal cage is installed in the cavity position of reactor, that port going deep into reactor inner chamber of this waveguide with should The inner chamber UNICOM of metal cage, described UNICOM refers to the connection in microwave channel meaning with through, and described quartz ampoule is to be erected at this The inside of metal cage, two described breather lines all penetrate the wall of this metal cage, and the locations of structures of the wall of this metal cage is between instead Answer the locations of structures between device inwall and quartz ampoule outer wall, and, booster pump, this booster pump is mixed with for supercharging pumping and urges in a large number Water after the degraded of agent particulate, its water inlet of this booster pump via ventilating water pipe and through described reactor wall with described instead The inner chamber answering device couples, and, the preposition prefilter of back flush type, this back flush type its water inlet of preposition prefilter is with described The delivery port of booster pump couples, and, back flush type doughnut membrane microfiltration filter, the preposition prefilter of described back flush type Its pure water inlet couples via the water inlet of first water purifying valve with this back flush type doughnut membrane microfiltration filter, and, instead Flushing type hollow-fibre membrane ultra filtration filter, described back flush type doughnut its pure water inlet of membrane microfiltration filter is via second Water purifying valve couples with the water inlet of this back flush type hollow-fibre membrane ultra filtration filter, this back flush type hollow-fibre membrane ultra-filtration filters The entrance point of its pure water inlet of device and the 3rd water purifying valve couples, and the water side of the 3rd water purifying valve is going out of outlet terminal water purification Water end (W.E.), and, catalyst underflow transition tank, this catalyst underflow transition tank is the tank body of a hollow, and this catalyst underflow transition tank is used In temporarily depositing the water body that catalyst concentration that its backwashing procedures of described filter discharged is higher, it is positioned at this catalyst underflow transition The catalyst underflow refluxing opening of its intracavity bottom of tank leads to the inner chamber of reactor, this catalyst underflow return valve via catalyst underflow return valve Being the valve body for this catalyst return flow line of switch control rule, described back flush type its outlet of sewer of preposition prefilter is via first Sewage valve lead to this catalyst underflow transition tank inner chamber, described back flush type doughnut its outlet of sewer of membrane microfiltration filter via Second sewage valve leads to the inner chamber of this catalyst underflow transition tank, and described back flush type hollow-fibre membrane its sewage of ultra filtration filter goes out Mouth leads to the inner chamber of this catalyst underflow transition tank via the 3rd sewage valve, and each described filter is used to retain catalyst particles, Each its outlet of sewer of described filter is all converted as by retaining the recycling delivery outlet of catalyst particles, and, described many Micro porous aeration head mutually assembles formation cluster-shaped micro porous aeration head cluster, and this cluster-shaped micro porous aeration head cluster is erected at institute vacantly Stating the lower area of reactor inner chamber, this cluster-shaped its bottom edge of micro porous aeration head cluster is vertical with described reactor inner chamber bottom surface To distance between 10 centimetres and 50 centimetres, this cluster-shaped micro porous aeration head cluster is edge and described reactor inner chamber arround it The lateral separation of sidewall is between 20 centimetres and 300 centimetres, and this its center of cluster-shaped micro porous aeration head cluster or center of gravity are positioned at The underface of described quartz ampoule, and, ozone sensor, the sampling port of this its probe tube of ozone sensor is adjacent to described tail gas Floss hole or probe into the inside of described exhaust port, and, ozone content display, ozone attention device or ozone content show Device and the composite structure of ozone attention device, this ozone sensor is via Article 1 cable and this ozone content display, ozone warning Device or ozone content display couple with the composite structure of ozone attention device, and, power-supply controller of electric, it is defeated for this ozone sensor Going out electric signal to couple with this power-supply controller of electric via Article 2 cable, this power-supply controller of electric is via Article 3 cable and described magnetron Coupling, this power-supply controller of electric couples with described air pump via Article 4 cable, and this power-supply controller of electric is can be received according to it Described electric signal carry out the power-supply controller of electric of power switch action, and, one group of ultrasonic transducer, this group of ultrasonic waves Can at least contain a ultrasonic transducer individuality by device, this group of ultrasonic transducer is used for radiating low-frequency ultrasonic waves, and this low frequency surpasses Sound wave refers to the frequency ultrasonic wave in 20kHz-60kHz scope, and this reactor inner chamber bottom surface is by periphery to central area gradually Hollow, described its gradient hollow is between 5 degree and 35 degree, and this group of ultrasonic transducer is to be installed in this reaction with attaching The lateral surface position of its part reactor diapire corresponding to hollow bosom of device inner chamber bottom surface or medial surface position, and, high Frequency vibration swings electric signal transmission cable, and the one group of ultrasonic transducer in one end of this higher-order of oscillation electric signal transmission cable and this couples, with And, higher-order of oscillation electric signal generator, the other end of described higher-order of oscillation electric signal transmission cable is sent out with this higher-order of oscillation electric signal Raw device couples, and, pH pops one's head in, and, pH analyzer, this pH probe is coupled to each other with pH analyzer, and this pH divides Analyzer and coupling with siren, this siren is for sending alarm to the pH value situation of transfiniting, and this pH probe is through reactor Top stretch into reactor inner chamber, and, through the micropore stainless steel sleeve that powder sintering process is made, this micropore stainless steel sleeve In cap for brush shape, this micropore stainless steel sleeve is positioned at reactor inner chamber, and down, this micropore is or not this micropore its blind end of stainless steel sleeve Upward, this its openend upward of micropore stainless steel sleeve joins with reactor head via buffering isolating pad in rust its openend of steel bushing Connecing, this pH pops one's head within its that part stretching into reactor inner chamber probes into this micropore stainless steel sleeve, this buffering isolating pad its Material is fluorubber or silicon rubber, and, two pairs of dry-reed type ball float level controllers, these two pairs of dry-reed type ball float level controllers All tops through reactor extend into the inner chamber of reactor, and a pair dry-reed type ball float level controller therein passes through a relay Device couples with the power cable of described water pump, and dry-reed type ball float level controller is passed through another relay and institute by therein another The power cable stating booster pump couples, and described sewage valve and described water purifying valve and described catalyst underflow return valve are all electromagnetism Valve.

Catalyst the most according to claim 1 intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external, it is characterised in that Its material of this metal cage is stainless steel, and, hole or its magnitude range of mesh of spreading all in this metal cage self structure are Between 0.5 centimetre and 3.0 centimetres.

Catalyst the most according to claim 1 intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external, it is characterised in that Distance between inwall and the outer wall of quartz ampoule of this metal cage is between 3.0 centimetres and 30.0 centimetres.

Catalyst the most according to claim 3 intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external, it is characterised in that Distance between inwall and the outer wall of quartz ampoule of this metal cage is between 10.0 centimetres and 20.0 centimetres.

Catalyst the most according to claim 1 intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external, it is characterised in that Its filter opening aperture of the preposition prefilter of described back flush type between 5 microns and 300 microns, described back flush type doughnut Its filter opening aperture of membrane microfiltration filter between 25 nanometers and 1000 nanometers, described back flush type hollow-fibre membrane ultra-filtration filters Its filter opening aperture of device is between 15 nanometers and 2 nanometers.

Catalyst the most according to claim 1 intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external, it is characterised in that This back flush type hollow-fibre membrane ultra filtration filter is at more than one back flush type hollow-fibre membrane ultra filtration filter by quantity Monomer is parallel with one another couples composition.

Catalyst the most according to claim 1 intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external, it is characterised in that This back flush type doughnut membrane microfiltration filter is at more than one back flush type doughnut membrane microfiltration filter by quantity Monomer is parallel with one another couples composition.

Catalyst the most according to claim 1 intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external, it is characterised in that At described back flush type doughnut its pure water inlet of membrane microfiltration filter and described back flush type hollow-fibre membrane ultra filtration filter Water inlet connecting pipeline on be equiped with second booster pump, this second booster pump is used for augmenting hydraulic pressure to meet described recoil Wash the intake pressure demand of formula hollow-fibre membrane ultra filtration filter.

Catalyst the most according to claim 1 intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external, it is characterised in that Offering sewage draining exit in the bottom of described reactor, this sewage draining exit is used for deslagging, removes contamination, and is equiped with blowdown at this Location for Sewage Valve, described blowoff valve is the valve controlled for blowdown.

Catalyst the most according to claim 1 intercepts the High-capacity photocatalytic wastewater degradation device that mechanism is external, it is characterised in that This micropore its wall thickness of stainless steel sleeve is between 3 millimeters to 30 millimeters, and this micropore its micropore size of stainless steel sleeve is at 0.5 micron Between 50 microns, this its thickness of buffering isolating pad is between 1 millimeter to 8 millimeter.