CN205258038U

CN205258038U - Dehydrator and cleaners and polishes to liquid manure mixture dehydration

Info

Publication number: CN205258038U
Application number: CN201521060313.2U
Authority: CN
Inventors: 张珂
Original assignee: Shanghai Yijie Environmental Protection Equipment Engineering Co Ltd
Current assignee: Shanghai Yijie Environmental Protection Equipment Engineering Co Ltd
Priority date: 2015-12-20
Filing date: 2015-12-20
Publication date: 2016-05-25
Anticipated expiration: 2025-12-20

Abstract

The utility model relates to a dehydrator and cleaners and polishes to liquid manure mixture dehydration. These cleaners and polishes are including the power device who is used for liquid manure to shift, the collection is mixing arrangement just, the collector, still include the dehydrator, the fluid infusion pipe that communicates this dehydrator and collector, condenser with this dehydrator of intercommunication. This dehydrator is enclosed by heat insulation layer and is equipped with the vaporizer that is used for carrying on solid -liquid separation in the fashioned box at it, the vaporizer including be used for temporary stock solution looks thing the appearance chamber, set up in the heating rod and the temperature sensor of its lower part, outer wall around this vaporizer is equipped with the steam chamber that communicates this vaporizer upper portion. The utility model discloses can save the power consumption in the cleaners and polishes working process.

Description

To dehydrator and the sanitary equipment of liquid manure mixture processed

Technical field

The utility model relates to a kind of harmless resource utilization dry type sanitary equipment, relates in particular to the dehydrator of these sanitary equipment.

Background technology

In patent documentation CN104172975A, a kind of harmless resource utilization dry type sanitary equipment are disclosed, comprise gathering-device; Condenser and dewater unit, this dewater unit comprises circulating pump, circulation pipe, vaporium, in its secondary separation stage, the evaporation tube heating of liquid phase thing in vaporium, is drained in steam pipe and flows away after generation steam. In order to reach the effect of gasification separation, need to keep to the long-time constantly heating of evaporation tube, this consumption for electric energy can not be ignored. This is the defect of prior art.

Summary of the invention

The technical problems to be solved in the utility model is to provide a kind of harmless resource utilization dry type sanitary equipment, dehydrator that reduces power consumption.

Harmless resource utilization dry type sanitary equipment of the present utility model, comprise the power set that shift for liquid manure; For the defecate collection mixing arrangement that absorbs liquid manure and mix with pulvis, for carrying out Separation of Solid and Liquid and collecting the collector of ight soil; It is characterized in that also comprising:

Dehydrator; Be communicated with the liquid supplementation pipe of this dehydrator and collector; With the condenser that is communicated with this dehydrator.

Described dehydrator, is surrounded by heat-insulation layer at it and is provided with the vaporizer for carrying out Separation of Solid and Liquid in the casing of moulding, and described vaporizer comprises the heating rod and the temperature sensor that are arranged at its underpart;

Be provided with the vapor chamber that is communicated with this vaporizer around the outer wall of this vaporizer.

Due to the heat transfer effect of the high-temperature steam in vapor chamber to vaporizer outer wall, liquid phase thing in vaporizer had just absorbed a large amount of heat energy before heating rod heating starts, thereby be heated to the required energy of boiling point and can greatly reduce, the utility model can be saved the power consumption in the sanitary equipment course of work.

Brief description of the drawings

Fig. 1 is the front view of harmless resource utilization dry type sanitary equipment of the present utility model.

Fig. 2 is the axonometric drawing of harmless resource utilization dry type sanitary equipment of the present utility model.

Fig. 3 is each parts annexation schematic diagram of harmless resource utilization dry type sanitary equipment of the present utility model.

Fig. 4 is the cutaway view of the blender of harmless resource utilization dry type sanitary equipment of the present utility model.

Fig. 5 is the cutaway view of the collector of harmless resource utilization dry type sanitary equipment of the present utility model.

Fig. 6 is the front view of the first embodiment of the dehydrator of harmless resource utilization dry type sanitary equipment of the present utility model.

Fig. 7 is the A-A cutaway view of Fig. 6.

Fig. 8 is the cutaway view of the second embodiment of the dehydrator of harmless resource utilization dry type sanitary equipment of the present utility model.

Detailed description of the invention

Now in conjunction with the accompanying drawings and embodiments the utility model is described in further detail.

Referring to Fig. 1 ~ Fig. 3, harmless resource utilization dry type sanitary equipment of the present utility model comprise just bucket 1, blender 2, collector 3, dehydrator 4, condenser 5, vacuum generator 6 and the vacuum controller 7 with pipeline communication, Fig. 3 is each parts annexation schematic diagram, and solid line has represented the pipeline being connected in therebetween. Vacuum controller 7 is provided with vacuum transducer 71, and it ensures the be not less than-65kPa of vacuum being produced by vacuum generator 6, thereby this place's vacuum is in sanitary equipment work, to shift the reliable power resources of liquid manure. In sanitary equipment, liquid manure is mainly gone through from the transfer of the first stage of the blender that just struggles against, the second stage from blender to collector and the phase III from collector to dehydrator, wherein, and the special defecate collection mixed process that claims of first stage; Second stage spy is called dump procedure; Phase III mainly refers to extract the process of liquid phase thing to dehydrator from collector, and spy is called fluid infusion process.

Coordinate and see that Fig. 3, Fig. 4, blender 2 are casings 20 of establishing in Give powder device 29 belows, to powder device 29 by forming to powder case 291 and meter 292, for inputting quantitative pulvis to casing 20; Casing 20 is communicated with atmosphere through breather valve 21; Be communicated with collector 3 through dump valve 22; 1 be communicated with just struggling against through defecate collection valve 23; Be communicated with vacuum controller 7 through vacuum valve 24; In blender 2, be provided with vacuum transducer 28, to ensure the be not less than-55kPa of vacuum in it, as the direct sources of power that absorbs liquid manure.

Defecate collection mixing starts from first power after an action of the bowels, coordinate and see Fig. 3, defecate collection valve 23 is opened, just the liquid manure in bucket is sucked by the negative pressure in casing 20, mixes with the pulvis descending slowly and lightly from top to bottom simultaneously, is deposited in the bottom of casing 20, then, close defecate collection valve 23, the mixture of pulvis and liquid manure produces the effect of sterilization, slaking and solidifying wadding through Ageing Treatment, and it is to use the prerequisite of defecate collection after an action of the bowels next time that the vacuum in blender returns to setting. After repeatedly facilitating, the liquid manure in casing 20 is more and more gradually, is also provided with upper and lower fluid level controller 27 in casing 20, and upper liquid level exceedes triggering liquid level limit protection, and now indicating function suspends use; Lower liquid level exceedes the interior liquid manure of triggering case can be by one of necessary condition of dump; The process that defecate collection mixes so far completes. Because the negative pressure for defecate collection is present in the chest of a sealing in advance, in defecate collection process, liquid manure is present in this sealing chest all the time, can not spray even a small amount of liquid manure to sanitary equipment outer surface, it is outside clean that sanitary equipment can keep, meanwhile, more can not pollute the environment that goes to toilet.

The power of dump procedure and fluid infusion process all derives from vacuum controller 7. Referring to Fig. 6 ~ Fig. 7, dehydrator 4 is casings 40 that insulation layer surrounds, the vapor chamber 42 that is provided with heating clamber 41 in casing 40, is communicated with heating clamber 41 tops, the outer Zheng Qi vacuum port 43 that is communicated with vapor chamber 42 that is provided with of casing 40; Referring to Fig. 5, in the casing 30 of collector 3, be provided with screen pack 31, casing cavity volume is divided into inner chamber 32 and exocoel 33 by it; Inner chamber 32 is communicated with heating clamber 41 through liquid supplementation pipe 35; When the vacuum valve 72 that the steam valve 51 being connected with condenser 5 cuts out, is communicated with vacuum controller 7 is opened, make-up valve 351 in liquid supplementation pipe 35 is opened, the negative pressure of vacuum controller 7 through steam vacuum port 43, vapor chamber 42, heating clamber 41, liquid supplementation pipe 35 is delivered in the inner chamber of collector 3, this power source that is fluid infusion process; Close when the open to atmosphere oxygen-adding valve 36 of often opening of company of being located on collector 3, the dump valve 22 being communicated with blender 2 is opened, and negative pressure can be delivered in blender 2 further, this power source that is dump procedure.

In inner chamber 32, be provided with upper and lower fluid level controller 321, after two, two necessary conditions of the necessary condition starting lower than lower liquid level triggering dump procedure all meet, dump procedure starts, and now, breather valve 21 is opened, and liquid manure is transferred to the exocoel of collector from blender.

Fluid infusion process refers to that liquid phase thing arrives inner chamber through filter screen, and is pumped via liquid supplementation pipe, arrive in the heating clamber of dehydrator, and solid formation is trapped in exocoel bottom because of the obstruct of screen pack, and therefore Separation of Solid and Liquid is accompanied by fluid infusion process and occurs. In the time that the collection valve 34 bottom being located at is opened, ight soil can be discharged from collector. In heating clamber 41, be provided with upper and lower fluid level controller 411, liquid level rises to liquid level and just triggers fluid infusion and stop, and fluid infusion process completes, and make-up valve is closed. Then, the vacuum valve being communicated with vacuum controller cuts out, and the steam valve being connected with condenser is opened, steam vacuum port 43 be in communication with the outside through condenser, prepare processed.

Heating clamber bottom is provided with for making this place's temperature guarantee temperature sensor 45 and the heating rod 46 at 100 DEG C, the vapor chamber 42 being communicated with heating clamber 41 tops is centered around the outer wall of heating clamber 41, processed need can make the liquid boiling in heating clamber by the power consumption energy critical heat of heating rod, gasification, in dehydrator except the higher solution of a part of concentration, the remaining rising water vapour that becomes flows into vapor chamber, the steam of the high temperature of disperse in vapor chamber is centered around the outer wall of heating clamber 41, it is large to Heat transfer amount, thereby the electric energy of heating rod 46 actual consumptions is few, the design of vapor chamber can be played effect of the energy of saving energy.

Solid-liquid primary separation in collector, dehydration in dehydrator separates solid-liquid again, meanwhile, because cause that the scatol of smelly feel and ammonia are all that dissolved solution is in water, when heating, also carried out gas-liquid separation, this provides prerequisite for follow-up deodorizing processing.

In the first embodiment of the present utility model, the condition of deodorizing processing is participation, initial reaction temperature and the catalyst converter that needs oxygen. Oxygen, from ambient atmosphere, pumps into by adding air pump 37, through the breather pipe 44 of collector, connection collector and heating clamber, arrives heating clamber top, and unnecessary air can arrive condenser through vapor chamber and be discharged from. Heating clamber top is provided with the heating rod 48 of catalyst converter 47 and contiguous this catalyst converter, heating rod 48 is by temperature increase to 230 DEG C, in heating rod 48, contain temperature sensor, be used for making reaction temperature to remain on 230 DEG C, this is the necessary condition that chemical reaction occurs, and because chemical reaction can be emitted large calorimetric, after startup catalytic reaction, temperature can exceed, can stop the power consumption of heating rod, the electric energy of these heating rod 48 actual consumptions is few. Catalyst converter is provided with catalyst, it is less than numerous particles of the sphere-like of 1mm for diameter,, like the limitation of existing cellular block, can not make catalytic reaction carry out, smelly odoring substance is thoroughly resolved into harmless scentless material, and this is also the necessary condition of catalytic reaction.

After liquid boiling in heating clamber, except the higher solution of a part of concentration, the remaining scatol that becomes rising water vapour and gaseous state and the mixture of ammonia, arrive the vapor chamber 42 being communicated with heating clamber top via catalyst converter, in this process, due to the effect of catalyst, the scatol that causes smelly feel containing in steam and ammonia and oxygen generation chemical reaction, be broken down into harmless nitrogen, carbon dioxide and water vapour, lose foul smell taste, and further arrive in condenser 5 and be condensed into liquid phase water and innocuous gas via the Zheng Qi vacuum port of being located at bottom half, be discharged in atmosphere.

Catalyst converter below is provided with bubble trap 49, for eliminating the foam producing when urine is seethed with excitement, damages catalyst in order to avoid it enters in catalyst converter, loses catalysis effect.

In the second embodiment of the present utility model, deodorizing processing is to carry out under vacuum condition, referring to Fig. 8, and the VOC catalysis being provided with heating clamber top, device box body 81 carries out catalytic reaction, also can reach the effect of removing stink.

Along with the carrying out of gas-liquid separation, the liquid level of vaporizer is more and more lower, in the time of its lower liquid level of low mistake, as triggering one of necessary condition of fluid infusion; In inner chamber 32, be provided with upper and lower fluid level controller 321, in the time that the liquid level of inner chamber did not have upper liquid level, while meeting as two, two conditions that trigger fluid infusion condition, trigger the fluid infusion process that starts simultaneously, make-up valve is opened, the solution that concentration is higher drops in inner chamber, mixes with the liquid phase thing of inner chamber, carries more scatol and ammonia, then be pumped in vaporizer, carry out gasification separation. So constantly back and forth, until dehydration all completes, and foul smell is removed.

The above is only preferred embodiment of the present utility model, not the utility model is done to any pro forma restriction, although the utility model discloses as above with preferred embodiment, but not in order to limit the utility model, any those skilled in the art, not departing from the scope of technical solutions of the utility model, when can utilizing the technology contents of above-mentioned announcement to make a little change or being modified to the equivalent embodiment of equivalent variations, in every case be the content that does not depart from technical solutions of the utility model, any simple modification of above embodiment being done according to technical spirit of the present utility model, equivalent variations and modification, all still belong in the scope of technical solutions of the utility model.

Claims

1. a dehydrator for harmless resource utilization dry type sanitary equipment, is surrounded by heat-insulation layer at it and in the casing of moulding, is provided with the vaporizer for making the liquid phase thing evaporation that is dissolved with solid formation and foul smell; It is characterized in that:

2. the dehydrator of harmless resource utilization dry type sanitary equipment as claimed in claim 1, is characterized in that:

Described vaporizer comprises for the cavity volume of temporary liquid storage phase thing and is arranged at heating rod and the temperature sensor of its underpart.

3. the dehydrator of harmless resource utilization dry type sanitary equipment as claimed in claim 2, is characterized in that also comprising:

Be located at the catalyst converter on this vaporizer top, this catalyst converter is less than the sphere-like catalyst of 1mm containing diameter;

For starting the heating rod of catalytic reaction, in it, be provided with temperature sensor; With

Carry out the breather pipe of catalytic reaction for delivery of oxygen.

4. the dehydrator of harmless resource utilization dry type sanitary equipment as claimed in claim 3, is characterized in that: described catalyst converter below is provided with froth breaker.

5. the dehydrator of harmless resource utilization dry type sanitary equipment as claimed in claim 2, is characterized in that also comprising:

Be located at the VOC catalyst converter on this vaporizer top.

6. harmless resource utilization dry type sanitary equipment, comprise the power set and the dehydrator that shift for liquid manure; It is characterized in that: this dehydrator is as described in one of claim 1 ~ 5.

7. harmless resource utilization dry type sanitary equipment as claimed in claim 6, it is characterized in that the described power set that shift for liquid manure comprise vacuum generator and be communicated with this vacuum generator in establish the vacuum controller of vacuum transducer.