1、沼氣從噴淋反應器的下端進入，穿過填料層后從頂部離開，進入后續處理階段，在沼氣管道上應設有流量計，以隨時監測管道內的沼氣流量，此外，在沼管道上還應安裝有沼氣成份分析儀，以定時監測沼氣中脫硫后沼氣內的硫化氫含量和甲烷含量。
1. Biogas enters from the lower end of the spray reactor and leaves from the top after passing through the packing layer. A flowmeter should be installed on the biogas pipeline to monitor the biogas flow in the pipeline at any time. In addition, a biogas composition analyzer should be installed on the biogas pipeline to monitor the content of hydrogen sulfide and methane in the biogas after desulfurization.
2、噴淋培養液從曝氣反應器泵出經換熱器后至噴淋反應塔上部進入，在實現噴淋循環的同時，通過換熱器使系統中培養液維持在一定的溫度環境下。
2. The spray culture liquid is pumped out from the aeration reactor through the heat exchanger and enters into the upper part of the spray reaction tower. While the spray circulation is realized, the culture medium in the system is maintained at a certain temperature through the heat exchanger.
在調試及運行的期間，先確定一個適合的溫度值。如果溫度下降，啟動換熱器熱水端的管道泵以升高溫度。當溫度升高到設定值時，停止管道泵。
During commissioning and operation, determine a suitable temperature value. If the temperature drops, start the pipe pump at the hot water end of the heat exchanger to increase the temperature. When the temperature rises to the set value, stop the pipeline pump.
3、風機采用了變頻控制，經過培養液曝氣反應器壁面上安裝的ORP(氧化還原電位計)來測定培養液之中的含氧量，并經過變頻器調節控制風機的出風量，以使培養液之中的含氧量控制于適當的范圍。
3. The fan is controlled by frequency conversion. The oxygen content in the culture medium is determined by ORP (oxidation-reduction potentiometer) installed on the wall of the aeration reactor for culture medium, and the air volume of the fan is controlled by the frequency converter to control the oxygen content in the culture medium in an appropriate range.
分析得出，這種控制方式的終端目的是控制進入沼氣中的氧濃度，如上所述，沼氣中混有不同的氧濃度，反應后的生成物是不相同的，反應后的產物可能是單質硫也可能會是稀硫酸，較為可能的會是兩者的混合物。
The analysis shows that the terminal purpose of this control mode is to control the oxygen concentration entering the biogas. As mentioned above, when the biogas is mixed with different oxygen concentrations, the products after reaction are different. The product after reaction may be elemental sulfur or dilute sulfuric acid, and more likely it will be a mixture of the two.
4、在培養基曝氣反應器壁上設置取樣口，人工采集培養基的pH值，判斷培養基中是否需要堿，堿的用量大小。通常來說，當終端產物為元素硫時，不需在培養基中加入堿。當終端產品為稀硫酸時，需要在培養基中加入堿，以保持培養基的中性要求。
4. A sampling port is set on the wall of the aeration reactor of the medium, and the pH value of the medium is collected manually to judge whether alkali is needed in the medium and the amount of alkali used. In general, when the end product is elemental sulfur, it is not necessary to add alkali to the medium. When the end product is dilute sulfuric acid, alkali should be added to the medium to maintain the neutral requirement of the medium.
5、理想的操作模式是每天更換一部分培養基。培養基的來源可通過沼液后的過濾和稀釋進行調節，調節方式須經試驗確定。由于沼液原料不同，置換量也需要現場試驗后確定，一般數據為每天更換數量的1/20至1/30。排出系統外的培養液需經過沉淀，以便在排出多余的培養液同時，從系統中帶走可能存在的單質硫等固體物質。不同的沼氣液可能不相同，使用何種營養液，具體要求和數量盡量是在調試時解決這個問題。大致的數量是每天更換1至2立方米左右。
5. The ideal operation mode is to change part of the medium every day. The source of culture medium can be adjusted by filtration and dilution after biogas slurry, and the adjustment mode must be determined by experiment. Due to the different raw materials of biogas slurry, the replacement amount also needs to be determined after field test, and the general data is 1 / 20 to 1 / 30 of the daily replacement quantity. The culture medium out of the system needs to be precipitated to remove the possible elemental sulfur and other solid substances from the system at the same time. Different biogas liquid may be different. The specific requirements and quantity of nutrient solution to be used should be solved during commissioning. The approximate quantity is about 1 to 2 cubic meters per day.
6、排渣采用了管道泵排渣的形式，經過過濾器以后把多余培養液送至污水處理車間。由此分析出，通常排放量與加入的培養液量相等。
6. After passing through the filter, the excess culture liquid is sent to the sewage treatment workshop. From this analysis, the discharge amount is usually equal to the amount of culture medium added.
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2020-08-27
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