Anaerobic bio-enhancement treatment method for cellulose ethanol wastewater
A cellulosic ethanol and anaerobic biological technology, which is applied in the field of anaerobic biological enhancement treatment, can solve the problems of high-concentration salt-containing organic wastewater treatment, no economically feasible treatment method, and increase the production cost of cellulosic ethanol. The effect of subsequent biochemical treatment, small investment, and difficulty reduction
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Embodiment 1
[0030] The treatment method of the present invention is used to treat the waste water of a domestic medium-scale test-scale cellulosic ethanol production plant. The main characteristics of the wastewater are: COD 129050 mg / L (chromium method, the same below), sulfate radical 9290 mg / L, inorganic salt 2.0%, pH 4.0.
[0031] The two-stage anaerobic enhanced microbial treatment process of the present invention was used to carry out laboratory treatment tests on the above wastewater. The wastewater treatment scale was 200 mL / h. The main experimental device configuration, operating conditions and treatment effects of each treatment unit are shown in Table 1. After being treated by the method of the present invention, the COD in the cellulosic ethanol wastewater can be reduced to less than 2000 mg / L, the amount of inorganic salts can be reduced to 1.0%, and the sulfate radical can be reduced to 10 mg / L, which greatly reduces the technical difficulty of subsequent wastewater treatment...
Embodiment 2
[0036] The treatment device of Example 1 was used to treat the same sewage as in Example 1, and the wastewater treatment effects obtained by changing the operating conditions of each treatment unit are shown in Table 2.
[0037] Table 2 The composition and treatment effect of the main processing units in Example 2.
[0038] Handling unit name Processing device scale and main components Main operating conditions and control parameters Inlet, outflow or treatment effect 1 The first anaerobic tank The contact process is adopted, the material is plexiglass, and the reactor volume is 100L. It mainly includes gas collecting hood, pool cover, pool body, feeding pipe, discharging pipe, mixing equipment and so on. The lower part continuously feeds water; the feed water is 200 mL / h of fiber ethanol raw water, and 800 mL / h of sludge liquid in sewage sedimentation tank; the total residence time of wastewater is 4.2 days; the volume load of feed water is 6.7 kgCOD / m ...
Embodiment 3
[0041] The treatment device of Example 1 was used to treat the same sewage as in Example 1, and the wastewater treatment effects obtained by changing the operating conditions of each treatment unit are shown in Table 3.
[0042] Table 3 Main processing unit configuration and processing effect of Example 3.
[0043] Handling unit name Processing device scale and main components Main operating conditions and control parameters Inlet, outflow or treatment effect 1 The first anaerobic tank The contact process is adopted, the material is plexiglass, and the reactor volume is 100L. It mainly includes gas collecting hood, pool cover, pool body, feeding pipe, discharging pipe, mixing equipment and so on. The lower part continuously feeds water; the feed water is 200 mL / h of cellulosic ethanol raw water, and 400 mL / h of sludge liquid in sewage sedimentation tank; the total residence time of wastewater is 6.9 days; the volume load of feed water is 6.6 kgCOD / m 3 ...
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