CN1127452C

CN1127452C - Method and equipoment for treating inidustrial effluent containing ammonium sulfate

Info

Publication number: CN1127452C
Application number: CN00111255A
Authority: CN
Inventors: 于祖荣; 梁孝成; 张秀文; 张立勤
Original assignee: XINHUA INDUSTRY AND TRADE Co Ltd SHANDONG
Current assignee: XINHUA INDUSTRY AND TRADE Co Ltd SHANDONG
Priority date: 2000-08-02
Filing date: 2000-08-02
Publication date: 2003-11-12
Anticipated expiration: 2020-08-02
Also published as: CN1336330A

Abstract

The present invention provides a method and a device for treating industrial wastewater containing ammonium sulfate. The device is composed of a pretreatment tank, a mother liquor tank, a crystallizing evaporator, a condenser and a centrifuge set. The pretreated wastewater is evaporated and crystallized by double effect, and is centrifugated by the centrifuge, and thus, nitrogenous fertilizer, namely ammonium sulfate, is prepared. The pretreated wastewater is centrifugated, and thus, the product is prepared. The overall process is completely and continuously operated, and the corrosion on the treatment devices is reduced. The treated wastewater can achieve the discharge standard of the environmental protection, and the environment pollution is reduced. The product has the advantages of stable quality, high content, easy transportation and convenient use. Simultaneously, the industrial production cost is correspondingly reduced.

Description

A kind of method of handling the trade effluent of sulfur acid ammonium

Technical field

The present invention relates to the processing of trade effluent, particularly a kind of trade effluent with the sulfur acid ammonium prepares the method and apparatus of nitrogenous fertilizer ammonium sulfate.

Background technology

At present, in chemical pharmacy industry, be easy to generate a large amount of trade effluents, what have contains a large amount of ammonium sulfate, such as the trade effluent that in the production process of pyrazolone material medicine, just very easily produces a large amount of sulfur acid ammoniums, owing to have serious corrodibility and the gluey unknown material (calling " colloid " in the following text) of many heavy-gravity, be difficult to handle in these waste water; Simultaneously because this type of waste water contains ammonium sulfate, can be used as nitrogenous fertilizer on the agricultural, but but be difficult for transportation and store, use also inconvenient, treatment process commonly used at present generally with waste liquid through evaporation, concentrate, natural then airing, the nitrogenous fertilizer quality instability that obtains like this, impurity is more, and the waste gas that produces in the evaporative process is more serious to equipment corrosion, therefore most producers generally all drain waste water, have also easily caused environmental pollution.

Summary of the invention

Purpose of the present invention is exactly at above-mentioned present situation, finds out a kind of method that can handle this type of trade effluent, and can turn waste into wealth, and preparation is easy to transport and nitrogenous fertilizer easy to use, improves the quality of products simultaneously, reduces the corrosion of equipment.。

The object of the present invention is achieved like this:

Handle the method for the trade effluent of sulfur acid ammonium, earlier waste water is carried out pre-treatment, and then evaporate, concentrate and separate with whizzer at last, its major technique characteristics are earlier waste water to be carried out pre-treatment, utilize economic benefits and social benefits crystallizing evaporator evaporative crystallization then, just the temperature of single-effect evaporator heating chamber is 110～120 ℃, and the temperature of last evaporator heating chamber is 65～75 ℃.

Pretreated mother liquor is introduced into last evaporator, changes in the first single-effect evaporator again, heats single-effect evaporator heating chamber just earlier, and after the first single-effect evaporator boiling, the waste gas with its generation changes the last evaporator heating chamber over to again, heats the mother liquor in the effect of end; When mother liquid concentration acquires a certain degree in imitating originally, feed liquid is pumped in the whizzer centrifugal, whizzer is constantly isolated ammonium sulfate crystallization (being product) and rarer mother liquor, and rarer mother liquor enters to pump in the mother liquor tank just again and continues to concentrate in the single-effect evaporator; Descend because of evaporation or the centrifugal liquid level that makes in just imitating, constantly mother liquor is changed over to just in imitating by the end and imitate.Like this through the economic benefits and social benefits crystallization and evaporations, the more stable and content of the ammonium sulfate crystallization quality that obtains is also than higher.

The corrosive exhaust gases condensation that the present invention can utilize the condenser that has vacuum jet pump to produce in will evaporating is removed, and reduces the corrosion of waste gas to equipment.

Because waste water has very strong acidity, particularly acidity is stronger after vaporizer concentrates, and the waste gas that evaporation produces also has very strong corrodibility.Having corrosive waste gas can suck in the condenser condensation by the vacuum that the vacuum jet pump that has on the condenser produces and remove; The heating chamber of crystallizing evaporator adopts corrosion resistant material, as the titanium material.

The pretreatment process of waste water is that waste water is injected the pre-treatment jar, microbubble generator is equipped with in the bottom of pre-treatment jar, the microbubble that microbubble generator sends penetrates direction and pre-treatment jar and vertical line direction certain angle, can make mother liquor under the effect of microbubble, produce rotation like this, simultaneously a large amount of microbubbles are attached on the colloid in the mother liquor, make colloid be subjected to the buoyancy of microbubble and rise to liquid level and, colloid is removed by the colloid device for filtering and collecting that is located at the liquid level place with mother liquor rotation.

A kind of device of handling the trade effluent of sulfur acid ammonium provided by the invention, form by pre-treatment jar, mother liquor tank, crystallizing evaporator and whizzer, it is characterized in that: crystallizing evaporator is imitated by first effect and end and is formed, the pre-treatment jar directly and last evaporator link, whizzer links with the first crystallizing evaporator of imitating, last evaporator connects the condenser that has vacuum jet pump, generally uses the dividing wall type condenser.

Described pre-treatment pot bottom is provided with microbubble generator, and microbubble that microbubble generator sends penetrates direction and pre-treatment tank diameter to vertical, and with the vertical line direction of pre-treatment jar certain angle is arranged, and the scope of angle is at 18～25 °.

The liquid level place, top of described pre-treatment jar is provided with the colloid device for filtering and collecting, is fixed on the pre-treatment jar tank skin; The colloid device for filtering and collecting mainly is made up of filter screen.

Advantage of the present invention is: to the centrifugal product that obtains, all complete operate continuouslys for the treatment of processes have reduced the corrosion to treatment facility simultaneously from the pre-treatment of waste water; Treated waste water can reach environmental emission standard, has reduced environmental pollution, and produces and be easy to transport and nitrogenous fertilizer-ammonium sulfate easy to use, simultaneously corresponding has also reduced industrial production cost.

Description of drawings

Fig. 1 is a setting drawing of the present invention;

Fig. 2 is the synoptic diagram of pre-treatment jar;

Fig. 3 is the vertical view of microbubble generator;

Fig. 4 is the sectional view of the production well of microbubble.

Among the figure, the 1st, the pre-treatment jar, the 2nd, first single-effect evaporator, the 3rd, last evaporator, the 4th, automatic centrifuge, the 5th, mother liquor tank, the 6th, condenser, the 7th, first single-effect evaporator heating chamber, the 8th, heating chamber is imitated at the end, the 9th, vacuum pump, the 10th, microbubble generator, the 11st, the colloid device for filtering and collecting, the 12nd, the production well of microbubble, L1～L14 is a pipeline, wherein L1 is the pipeline that first single-effect evaporator waste gas enters last evaporator heating chamber 8, and L2 enters the steam-pipe of single-effect evaporator heating chamber 7 just, and L3 is condensed water discharge pipe road in the first single-effect evaporator heating chamber 7, L4 is that condensed water discharge pipe road in the heating chamber 8 is imitated at the end, L5 is that the mother liquor after last evaporator 3 preliminary the concentrating enters the pipeline of single-effect evaporator 2 just, and L7 is the pipeline that the isolated rarer mother liquor of whizzer enters mother liquor tank 5, and L8 pumps into further spissated pipeline in the first single-effect evaporator 2 with the mother liquor in the mother liquor tank 5, L9 is that the waste gas in the last evaporator 3 enters the pipeline in the condenser 6, vacuum pump 9 connects with condenser 6 by L10, and L11 is that the waste gas of last evaporator 3 is through condensed condensed water discharge pipe road, L12, L13 is respectively the water coolant inlet and outlet piping of condenser 6, enters last evaporator 3 through pretreated mother liquor by L14.

Embodiment

Manufacture and design the production equipment that a cover is handled the trade effluent of sulfur acid ammonium by accompanying drawing 1, wherein, 2 and 3 all is vertical crystal type crystallizing evaporator, F=90M ², heating chamber is the titanium material, other position is 316L, and the 4th, the automatic centrifuge of HY8000 type, the 5th, K500 retort, band insulation interlayer and stirring, the 6th, dividing wall type condenser, F=162M ²Just the single-effect evaporator vapor pressure maintains 0.35 ± 0.02MPa; With the waste water of concentration 20%, output can reach 2 tons/hour, and the waste water output with 40% can reach 4.5 tons/hour.

Pretreated mother liquor enters last evaporator 3 through L14, and in L5 changes just single-effect evaporator 2 over to, when reaching certain liquid level originally in the single-effect evaporator 2, heating is single-effect evaporator heating chamber 7 just, just single-effect evaporator 2 boiling back waste gas enter last evaporator heating chamber 8, mother liquor in the heating last evaporator 3, just descend because of evaporation or the centrifugal liquid level that makes in the single-effect evaporator 2, by constantly mother liquor being changed over to single-effect evaporator 2 just in the last evaporator 3, mother liquor through single-effect evaporator 2 evaporations just pumps in the automatic centrifuge 4 centrifugal, automatic centrifuge 4 is constantly isolated ammonium sulfate crystallization and rarer mother liquor, and mother liquor enters to pump in the mother liquor tank 5 just again and continues to concentrate in the single-effect evaporator 2.The corrosive exhaust gases that produces in the last evaporator 3 is constantly sucked in the dividing wall type condenser 6 by the vacuum of being come by corrosion resistant vacuum jet pump 9, L12 is the rising pipe of water coolant, L13 is the water inlet pipe of water coolant, pass back into the circulating water pool after L12 goes the water cooling tower cooling and reuse, the corrosive exhaust gases that produces in the last evaporator 3 flows into the water drain from L11 through the water of condensation that 6 condensations of dividing wall type condenser go out.

Claims

1, a kind of method of handling the trade effluent of sulfur acid ammonium, earlier waste water is carried out pre-treatment, and then evaporate, concentrate and separate with whizzer at last, it is characterized in that: imitate with the end through just through pretreated waste water and imitate the double-effect evaporation crystallization, just the temperature of single-effect evaporator heating chamber is 110～120 ℃, and the temperature of last evaporator heating chamber is 65～75 ℃.

2, method according to claim 1, it is characterized in that: pretreated mother liquor enters last evaporator, change over to again in the first single-effect evaporator, when reaching certain liquid level in imitating originally, at first single-effect evaporator heating chamber external admission valve heating, the back of single-effect evaporator boiling just waste gas enters the last evaporator heating chamber, mother liquor during imitate at the heating end, because of evaporating or pumping into the whizzer separation liquid level is descended in just imitating, imitate by constantly mother liquor being changed over to just in the effect of end, when mother liquid concentration acquires a certain degree in imitating originally, pump in the whizzer feed liquid centrifugal, whizzer is constantly isolated ammonium sulfate crystallization and rarer mother liquor, and rarer mother liquor enters to pump in the mother liquor tank just again and continues to concentrate in the single-effect evaporator.

3, method according to claim 1 is characterized in that: described pre-treatment is in the pre-treatment jar, produces microbubble by microbubble generator, and colloid is removed by the colloid device for filtering and collecting to liquid level then with bubble is floating.