CN1119177A

CN1119177A - Method and equipment for making manure by sewage treatment

Info

Publication number: CN1119177A
Application number: CN95106299A
Authority: CN
Inventors: 张宇舟; 张宇舒; 张金禄; 高桂华
Original assignee: Individual
Current assignee: Individual
Priority date: 1995-06-27
Filing date: 1995-06-27
Publication date: 1996-03-27
Anticipated expiration: 2015-06-27
Also published as: CN1062544C

Abstract

The method for producing fertilizer by sewage treatment includes introducing air into living sewage, filtering through boiler flue dust and adding ferment to the boiler flue dust capturing dirt, and fermentation, and features high efficiency, and simple apparatus.

Description

A kind of method and apparatus of making manure by sewage treatment

The invention belongs to sewage treatment area, also belong to the fertilizer preparation field.

About 200,000,000 tons of China's discharging every day industry and sanitary sewage wherein do not have more than 90% through any processing, and directly polluted-water is above 2,000,000,000 meters ³The municipal sewage plant of present bent type belongs to second-stage treatment, is basic means with physics biochemical process and gravitational settling method, by suspended matter and the colloidalmaterial in processing steps such as precipitation, the aeration removal water.Because 99.9% (weight) is water in the sewage, this treatment plant takes up an area of huge, adds the sewage transport engineering, makes the cost of urban sewage treatment system very expensive.In addition, this second-stage treatment of process can't be removed and is dissolved in pollutants in sewage-mineral nutrient, and draining still has the problem of nutrient loss and polluted-water.Tertiary treatment adopts quartz sand, cobble etc. for the filter bed material filters, activated carbon adsorption, can address this problem, but recoil regularly and regeneration, and involve great expense, in the world up to the present, what really put into operation is considerably less.

On the other hand, for improving crop yield, the very expensive chemical fertilizer of a large amount of prices is used in the soil year after year, causes soil compaction, dysplasia.

Again on the one hand, be the minimizing topsoil, the annual boiler smoke of collecting from the boiler exhaust gas that burns coal cinder in the whole nation reaches tens million of tons, and these cigarette ashes cause secondary pollution unavoidably in stacking, transportation.

The objective of the invention is to solve the problems referred to above of prior art, a kind of method and equipment used that utilizes boiler smoke to dispose of sewage to produce fertilizer is provided.

Method of the present invention for sanitary sewage through boiler smoke filter water purification, the boiler smoke of holding back dirt is added ferment fermentation makes fertilizer.

The preferred especially sewage of this method charged into air earlier before filtering through boiler smoke, impel the phosphoric acid salt crystallization that is dissolved in the sewage to separate out, and for later fermentation step provides required dissolved oxygen content, and particularly advantageous is sewage through two-stage air water Mixing and aeration at least.In addition, in order to remove bigger solid dirt in advance, sewage just can be filtered through a grid earlier, the grid mesh can be at 10 * 10～20 * 20mm, the comb formula device that also available spacing 5～15mm parallel metal bar is made.

The used boiler smoke of present method particularly carbon content is 30～60% (weights), and all the other main chemical compositions of ash are silicon-dioxide, aluminium sesquioxide and part trace element, granularity 0.2-2 millimeter, the cigarette ash that the grate firing boiler smoke evacuation of available burning coal cinder is collected.Also can use and make the cigarette ash bedding and padding as straw.40～60 millimeters of preferred pad bed thickness, thick 400～800 millimeters of filtering layer, sanitary sewage flows through filtering layer, bed course from top to bottom with 10～30 meters/hour speed.

Particularly the boiler smoke of holding back dirt can be added wood chip or the high carbon species of sugared slag class in present method, fermentation raw material is contained:

Wood chip or the high carbon species 10～25% of sugared slag class (weight)

Ferment 0.1-0.5% (weight)

Water 40～60% (weight)

Filtrate, bedding and padding, dirt 25～40% (weight)

30～60 ℃ of leavening temperatures, fermentation time be more than 15 days, particularly 15～20 days, to chocolate, do not have stink, make fertilizer when bearing white hair, stirs between yeast phase 2～3 times.

Method equipment used of the present invention comprises strainer and mixed fermentation pond, particularly also can comprise gas and water mixer.

In a preferred scheme of the present invention, equipment of the present invention comprises the preliminary filter of being with grid, multistage gas and water mixer, sewage is sent into the pump of gas and water mixer from the preliminary filter, reception is from the sewage lagoon of the sewage of gas and water mixer, the strainer of boiler smoke filtering layer is housed, sewage is sent into the fermentation vat of filtrate of holding back dirt of taking out in the pump of strainer and the splendid attire strainer etc. from sewage lagoon.

Major advantage of the present invention is as follows:

1, the treatment of wastes with processes of wastes against one another, boiler smoke, sanitary sewage, wood chip etc. all are refuses, and cause environmental pollution, filter sewage with boiler smoke, have both made full use of waste material, again the comprehensive regulation environment, existing social benefit has an economic benefit again.

2, become useless and enlarge the source of manure into fertile, the fertilizer that this method is produced contains multiple nutritional components, can also improve the soil;

3, raw material sources are extensive, and cheap, product fertilizer demand amount is big;

4, sewage is processed in flowing fast, and efficient height, effective, strainer do not need back flushing, is convenient to operation and management;

5, can build sewage work at the rivers discharge outlet place of existing sewage with the present invention, take up an area of and lack, device structure is simple, and efficient height, profitable is implemented easily.

Further specify the present invention below by drawings and Examples.

Fig. 1 is that a kind of boiler smoke of the present invention filters the process flow diagram that sanitary sewage is produced fertilizer.

Fig. 2 is the synoptic diagram of the used a kind of multistage inhaling type aerator of the present invention.

Number in the figure 1 is the preliminary filter, and 2 is pump, and 3 is multistage inhaling type aerator, 4 is sewage lagoon, and 5 is pump, and 6 is pressure filter, 7 are the mixed fermentation pond, and 8 is waste pipe, and 9 is pure water pipe, 11 is sewage inlet, and 12 is the one-level suction opening, and 13 is first order jet nozzle, 14 is secondary nozzle, and 15 is three grades of nozzles, and 16 is three grades of suction openinies, 17 is the level Four nozzle, and 18 is the secondary suction opening.

Embodiment 1

Town domestic sewage discharge outlet about 2000 tons of existing day water displacement is set up treatment plant.The major equipment that needs has; 2 of submerged sewage pumps, 2 of in-line pumps; 〉=10 meters ³One of sewage lagoon; 2 of Φ 2000 * h2600mm pressure filters; Filtering velocity get 10-20 rice/hour; 5 meters ³6 of fermentation vats; (solid amount TS)≤1000 mg/litre of sewage inlet; The TS of draining≤50 mg/litre, 2～3 tons in daily output fertilizer.

Embodiment 2

Sanitary sewage is just squeezed into one or more multistage inhaling type aerators (3) by pump (2) after the filter through the preliminary filter (1) of band grid, water is repeatedly with the flow velocity of 15～20 meter per seconds nozzles at different levels (13 from device (3), 14,15,17) ejection, form eddy current, and generation negative pressure, with air from suction opening (12,18,16) suck, moment the air water thorough mixing, finish the transfer of oxygen in water rapidly, make dissolved oxygen (DO) 〉=6 mg/litre, impel salt soluble in water to form insoluble salt compound, multistage gas and water mixer (3) external diameter is greater than diameter of conveying pipe, axially long only about 1 meter, mixed water is to sewage lagoon (4), squeeze into pressure filter (6) by pump (5), the straw bed course (the long 20-40 millimeter of straw) of 40-60 mm thick and the boiler smoke filtering layer of 400-800 mm thick are housed in the strainer (6), described filtrate is the boiler smoke that the content of the grate firing boiler smoke evacuation collection of burning coal cinder accounts for cigarette ash total amount 30-60%, all the other main chemical compositions of ash are silicon-dioxide, aluminium sesquioxide and part trace element, surmise the 0.2-2 millimeter, the sewage that comes self-pumping (5) flows through filtering layer from the top down with 10～30 meters/hour filtering velocity, bed course, because contact, cohesion, permeation filtration, membrane filtration and adsorption, suspended matter in the sanitary sewage, gelatinoid and be partly dissolved material and be trapped, be adsorbed in the filtering layer, the purification that is higher than second-stage treatment is discharged through water-freeing arrangement, send into water body or farmland, when strainer pressure reduction increases, after water outlet is reduced to a certain degree, it is saturated to be considered as filtrate, not back flushing, but stop to send water, after treating that water is got rid of, with the filtrate in the strainer, bedding and padding and dirt are all sent into mixed fermentation pond (7), filtrate, bedding and padding, dirt accounts for fermentation raw material gross weight 25～40%, mix for No. 3 with wood chip that accounts for fermentation raw material gross weight 10～25% or the high carbon species of sugared slag class and the ferment that accounts for fermentation raw material gross weight 0.1-0.5%, make the water content of raw material account for the 40-60% of gross weight, be heated to 30 ℃ with top fermentation, in the time of 40-60 ℃, (need 5-6 days approximately) and stir 1-2 time, build with plastic film, became chocolate in 15-20 days, no stink, it is complete to make nutriment in a fertilizer when bearing white mao, the fertilizer that fertilizer efficiency is steady and long.

Claims

1, a kind of method of making manure by sewage treatment, it is characterized in that with sanitary sewage through boiler smoke filter water purification, the boiler smoke of holding back dirt is added ferment fermentation makes fertilizer.

2, method as claimed in claim 1 is characterized in that charging into air earlier in sewage, filters described sewage with boiler smoke then.

3, method as claimed in claim 1 is characterized in that sewage is earlier through a grid or the filter just of combing.

4, method as claimed in claim 1 is characterized in that boiler smoke carbon content 30～60% (weight), and all the other main components of ash are silicon-dioxide, aluminium sesquioxide and trace element, granularity 0.2-2 millimeter.

5, method as claimed in claim 1 is characterized in that using the straw bedding and padding below the boiler smoke, thick 400～800 millimeters of filtering layer, thick 40～60 millimeters of bed course.

6,, it is characterized in that sanitary sewage flows through filtering layer, bed course from top to bottom with the speed of 10～30 meter per seconds as the method for claim 1 or 5.

7, method as claimed in claim 1 is characterized in that the boiler smoke that will hold back dirt adds wood chip or the high carbon species of sugared slag class, contains fermentation raw material:

Wood chip or the high carbon species 10～25% of sugared slag class (weight)

Ferment 0.1-0.5% (weight)

Water 40-60% (weight)

Filtrate, bedding and padding, dirt 25-40% (weight)

8, as the method for claim 1 or 7, it is characterized in that described leavening temperature is 30～60 ℃, fermentation time is more than 15 days.

9, the method equipment used of one of a kind of claim 1 to 8 is characterized in that comprising gas and water mixer, strainer and fermentation vat.

10, equipment as claimed in claim 9, it is characterized in that comprising the preliminary filter of band grid or comb, multistage gas and water mixer, sewage is sent into the pump of gas and water mixer from the preliminary filter, reception is from the sewage lagoon of the sewage of gas and water mixer, the strainer of boiler smoke filtering layer is housed, sewage is sent into the fermentation vat of filtrate of holding back dirt of taking out in the pump of strainer and the splendid attire strainer etc. from sewage lagoon.