A kind of high ammonia nitrogen wastewater treatment device and method
A waste water treatment, high ammonia nitrogen technology, applied in the direction of biological water/sewage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc., can solve the problems of low denitrification efficiency, effluent ammonia nitrogen not up to standard, etc., and achieve high exposure The effect of volume
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Embodiment 1
[0083] In this embodiment, a high ammonia nitrogen wastewater treatment device is used for wastewater treatment. The high ammonia nitrogen wastewater treatment device comprises a biological reaction zone 100, a separation zone 200 and a sludge activation zone 300, wherein the volume ratio of the first aerobic zone 120 and the second aerobic zone 130 in the biological reaction zone 100 is 1:1.5, The ratio of the lower cross section to the upper cross section at the top of the central cylinder is 1:1.5.
[0084] A certain food wastewater was pretreated to obtain sewage A. The water quality COD was 100-200mg / L, ammonia nitrogen was 50-60mg / L, total nitrogen was 60-80mg / L, and the biodegradability of the wastewater was good. B / C>0.4, The specific processing steps are as follows:
[0085] S10. Sewage A enters the central cylinder 110 of the biological reaction zone 100 upwards through the water distributor 112, and the aeration device 111 is turned on to control the oxygen content...
Embodiment 2
[0093] The basic content of this embodiment is the same as that of Embodiment 1, except that the volume ratio of the first aerobic zone 120 to the second aerobic zone 130 in the biological reaction zone 100 is 1.3:1.5, and the lower horizontal line at the top of the central cylinder The ratio of section to upper cross section is 1:1.3.
[0094] Sewage A is obtained after pretreatment of industrial wastewater. The COD of the water is 800-1000mg / L, the ammonia nitrogen is 100-120mg / L, the total nitrogen is 100-120mg / L, and the biodegradability of the wastewater is poor B / C<0.3. The processing steps are as follows:
[0095] S10. Sewage A enters the central cylinder 110 of the biological reaction zone 100 upwards through the water distributor 112, and the aeration device 111 is turned on to control the oxygen content of the water body to 2-3mg / L. The sewage A is aerobic in the first aerobic zone 120 Remove COD to obtain sewage B that removes most of COD;
[0096] S20, the sewage...
Embodiment 3
[0103] The basic content of this embodiment is the same as that of Embodiment 1, except that the volume ratio of the first aerobic zone 120 to the second aerobic zone 130 in the biological reaction zone 100 is 1.5:1.1, and the lower horizontal line at the top of the central cylinder The ratio of the section to the upper cross section is 1:1.1.
[0104] A certain pesticide wastewater was pretreated to obtain sewage A. The water quality COD was 800-1000mg / L, ammonia nitrogen was 50-60mg / L, total nitrogen was 80-100mg / L, and the biodegradability of the wastewater was poor 0.3<B / C <0.4, the specific processing steps are as follows:
[0105] S10. Sewage A enters the central cylinder 110 of the biological reaction zone 100 upwards through the water distributor 112, and the aeration device 111 is turned on to control the oxygen content of the water body to 2-3mg / L. The sewage A is aerobic in the first aerobic zone 120 Remove COD to obtain sewage B that removes most of COD;
[0106]...
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