經濟部中央標準局員工消费合作杜印製 401380 A7 B7 五、發明説明（4 ) 〔發明之詳細說明〕 〔發明所屬之技術領域〕 本發明爲關於在下水處理設施中所發生之下水污泥， 和在屎尿處理設施中所發生之屎尿污泥等之含有機質污泥 中，將含有生石灰之脫水材料混合並脫水，且令脫水後之 固形成分於水泥原料中混入並處理之含有機質污泥的處理 方法。 〔先前之技術〕 先前，下水污泥等之含有機質污泥已被以各種方法處 理，於特開平3 — 9 8 7 0 0號公報中，揭示將作爲脫水 材料之生石灰、假燒白雲石、水沈澱物、高爐爐渣於下水 污泥中混合混合，並將污泥脫水後之固形成分於水泥原料 中混入並處理，且將脫水時所發生之氣體投入之水泥焙燒 工程中之方法。 又，此種污泥之脫水處理設備自以往爲在每個下水處 理場中設置，對發生之污泥每次進行處理。 〔發明所欲解決之課題〕 於上述之處理方法中，爲經由令脫水材料中之生石灰 成分與污泥中之水分如下反應，且污泥中的水分爲被此水 和反應所消耗，或者經由反應熱而蒸發’而令下水污泥脫 水。Duo printed 401380 A7 B7 for employee cooperation of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (4) [Detailed description of the invention] [Technical field to which the invention belongs] The present invention relates to sewage sludge that occurs in sewage treatment facilities. Organic sludge containing organic sludge, such as fecal urine sludge that occurs in fecal urine treatment facilities, is mixed with dehydrated material containing quicklime, and organic sludge containing dehydrated solids is mixed and processed in cement raw materials. Approach. [Previous Technology] Previously, organic sludge including sewage sludge has been treated by various methods. In Japanese Unexamined Patent Publication No. 3-9878, quicklime, pseudo-burned dolomite, Water sediment and blast furnace slag are mixed in sewage sludge, and the solid content of the dewatered sludge is mixed and treated in the cement raw materials, and the gas generated during dehydration is put into the cement roasting process. In addition, such sludge dewatering treatment equipment has been installed in every sewage treatment plant in the past, and the generated sludge is treated every time. [Problems to be Solved by the Invention] In the above-mentioned treatment method, the reaction of the quicklime component in the dehydrated material with the moisture in the sludge is as follows, and the moisture in the sludge is consumed by the water and the reaction, or through The reaction heats and evaporates', which dewaters the sewage sludge.
CaO + HzO-^Ca (OH) 2 本紙張尺度適用中國國家標準（CNS ) A4規格（21〇Χ297公釐〉 (請先閱讀背面之注意事項再填寫本頁)CaO + HzO- ^ Ca (OH) 2 This paper size applies to Chinese National Standard (CNS) A4 (21〇 × 297 mm) (Please read the precautions on the back before filling this page)
、tT -4- 經濟部中央標準局員工消費合作社印裝 A7 ______B7 五、發明説明（2 ) 然而，脫水材料爲生石灰時，因生石灰爲高價故有經 費上之問題，又，將脫水後之固形成分使用作爲水泥原料 上，因成分相差懸殊，故有必須進行成分調整之問題。 再者，以往，因爲即使在污泥發生量較少之處理場中 ，亦設置各個脫水處理設備，故在中小規模之下水處理設 施中，乃有脫水處理設備之運轉率低，且處理費用較貴之 問題。 本發明爲鑑於此類先前問題，以提供可令下水污泥和 屎尿污泥等之含有機質污泥適當地脫水，且令含有機質污 泥之脫水後的固形成分可就其原樣容易地使用作爲水泥原 料，不會令水泥製品之性能降低，可經濟地、有效率地處 理含有機質污泥，並且提高脫水處理設備之運轉率，可削 減處理費用之處理方法爲其目的。 〔解決課題之手段〕 爲了解決如上述之先前問題，並達成所期目的之本發 明特徵爲令含有生石灰之脫水材料於含有機質污泥中混合 並脫水，並將前述污泥脫水後之固形成分於水泥原料中混 入並處理之含有機質污泥之處理方法中，前述脫水材料爲 由水泥焙燒系之懸吊預熱器中分取，爲加熱水泥原料所得 含有生石灰之中間工程品。 又，具有令脫水材料與污泥混合脫水之脫水處理設備 作成可移動，並使該脫水處理設備於必要之場所中移動進 行脫水處理之其他特徵，此時，令脫水處理設備搭載於卡 本紙張尺度適用中國國家標準（CNS > Α4規格（210X297公釐） (請先聞讀背面之注意事項再填寫本頁) 、"τ -5- 經濟部中央標準局員工消費合作社印製 401380 五、發明説明（3 ) 車上，並以該卡車上進行脫水處理爲較佳，且此脫水處理 設備以具備裝脫水材料加料斗、裝污泥加料斗，令前述兩 加料斗所供給之脫水材料與污泥混合攪拌之原料混合機， 將來自前述兩料斗之脫水材料及含有機質污泥定量供給至 該原料混合機之定量供給機，及將脫水處理後之固形成分 排出之排出用運轉機爲較佳》 再者’將脫水處理設備及加熱水泥原料所得之含有生 石灰之中間工程品，搬送至含有機質污泥發生地，並於該 污泥發生地進行脫水處理，將該脫水處理後之固形成分搬 送至水泥工廠並混入水泥原料爲較佳。 尙，含有機質污泥除了爲在含有機質處理設施中所發 生之含有機質污泥，和在屎尿處理設施中所發生之屎尿污 泥以外’可運用於家庭廢水處理、產業廢水處理、疏浚水 上飛機處理等具有臭氧之含有機質污泥。 〔發明之實施形態〕 其次以圖面說明本發明之實施形態。 首先，若說明本發明之第一實施形態，則於水泥工廠 爲如圖1所示，水泥原料L爲由原料貯藏場1，通過原料 乾燥機2、原料粉碎機3、原料槽4，供給至水泥焙燒系 之懸吊預熱器中。尙，水泥原料L爲由石灰石、粘土、矽 石、鐵原料等所組成，將其加熱所得之中間工程品Q(後 述）一般爲比生石灰廉價。 水泥焙燒系之懸吊預熱器爲由具有複數段之旋風分離 本紙張尺度適用中國國家標準（CNS ) A4規格（2丨0 X Μ公釐） (請先閱讀背面之注意事項再填寫本頁)、 TT -4- Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs A7 ______B7 V. Description of Invention (2) However, when the dehydrated material is quicklime, there is a problem in terms of funding due to the high price of quicklime, and the dehydrated solid form When using ingredients as cement raw materials, there is a problem that the composition must be adjusted because the ingredients are very different. In addition, in the past, because each dehydration treatment equipment was installed even in a treatment site with a small amount of sludge, in the small and medium-scale water treatment facilities, the operation rate of dehydration treatment equipment was low, and the treatment cost was relatively low. Expensive question. In view of such a prior problem, the present invention is to provide organic sludge containing sewage sludge, fecal urine sludge, and the like to be properly dehydrated, and solid matter after dehydration containing organic sludge can be easily used as it is. Cement raw materials will not reduce the performance of cement products, can economically and efficiently treat organic sludge, and improve the operation rate of dehydration processing equipment, and can reduce processing costs for its purpose. [Means for solving problems] In order to solve the above-mentioned problems and achieve the desired object, the present invention is characterized in that the dehydrated material containing quicklime is mixed and dehydrated in sludge containing organic matter, and the solid content of the sludge after dehydration is dehydrated. In the organic sludge-containing treatment method mixed and treated in cement raw materials, the aforementioned dewatering material is separated from a suspension preheater of a cement roasting system, and is an intermediate engineering product containing quicklime obtained by heating the cement raw materials. In addition, it has other features that the dewatering processing equipment that allows dewatering materials and sludge to be mixed and dewatered can be moved, and the dewatering processing equipment can be moved in a necessary place to perform dewatering processing. At this time, the dewatering processing equipment is mounted on cardboard paper. Standards are applicable to Chinese national standards (CNS > Α4 specifications (210X297 mm) (please read the notes on the back before filling out this page)) " τ -5- Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 401380 5. Description of the invention (3) It is better to carry out dehydration treatment on the truck, and the dehydration treatment equipment is provided with a dehydration material charging hopper and a sludge charging hopper, so that the dewatering materials supplied by the two hoppers described above and The raw material mixer for sludge mixing and mixing, the quantitative supply machine for quantitatively supplying the dehydrated material and organic-containing sludge from the two hoppers to the raw material mixer, and the discharge operation machine for discharging solid components after dehydration treatment are compared. "Good" Furthermore, the intermediate engineering products containing quicklime obtained from dehydration treatment equipment and heating cement raw materials will be transported to organic sludge containing hair. It is better to carry out dehydration treatment at the place where the sludge occurs, and it is better to transport the solids after dehydration treatment to a cement factory and mix the cement raw materials. Organic sludge and organic sludge with ozone, such as domestic sewage treatment, industrial wastewater treatment, dredging seaplane treatment, etc. can be used in addition to fecal urine sludge generated in feces treatment facilities. [Implementation Mode of the Invention] Next The embodiment of the present invention will be described with reference to the drawings. First, if the first embodiment of the present invention is described, as shown in FIG. 1 in a cement factory, a cement raw material L is obtained from a raw material storage site 1 and passed through a raw material dryer 2 and a raw material. The pulverizer 3 and the raw material tank 4 are supplied to the suspension preheater of the cement roasting system. Alas, the cement raw material L is composed of limestone, clay, silica, iron and other raw materials, and the intermediate engineering product Q obtained by heating (Described later) Generally cheaper than quicklime. The suspension preheater of the cement roasting system is separated by a cyclone with a plurality of sections. This paper applies Chinese national standards. Standard (CNS) A4 specification (2 丨 0 X MM mm) (Please read the precautions on the back before filling this page)
.1T -6- 經濟部中央標準局貝工消費合作社印製 _ __B7____ 五、發明説明（4 ) 器5、 6、 7、 8、假燒爐9所構成，旋轉爐10之排氣 爲以假燒爐9、旋風分離器8、7、6、5之順序供給。 其後於最上段之旋風分離器5中投入水泥原料1 ’且令此 水泥原料L爲到達最下段之旋風分離器8爲止地於8 5 0 °C〜 9 0 0°C加熱，並經由水泥原料L中石灰石之脫碳酸 化而如下述生成生石灰。 C a C〇3~^C a 0 + C〇2 尙，至最下段旋風分離器8爲止之中間工程品Q的主 要成分，其一例爲S i〇2 19 . 0 % , A 1 2 0 3 4.3%、F e 2 Ο 3 2.7%、C a Ο 60.5%、 M g Ο 1 . 5%，爲充分含有生石灰。又，於中間工程 品Q中，含有約0 . 5%之未燃燒碳。 其後，由最下段之旋風分離器8，將含有生石灰之中 間工程品Q供給至旋轉爐1 〇，並在最下段之旋風分離器 8之下方出口設置分取氣門2 0，透過分取氣門2 0而分 取指定量的中間工程品Q。其後，將所分取之中間工程品 Q通過水冷式冷卻器2 1、輸送機2 2、運出槽24，並 經由搬送車2 5搬送至下水處理設施之污泥處理場。尙， 圖1中’ 2 3爲氣塞加料器，而於運出槽2 4中裝備有集 塵機。 另一方面，於下水處理設施等所附帶之污泥處理場中 ’如圖2所示’下水污泥（脫水餅）s爲由脫水裝置3 1 ，通過定量供給機3 2，投入原料混合機4 〇。尙，下水 污泥S爲含有約8 0%之水分。又，含有生石灰之水泥中 本紙張尺度適用中國國家標準（CNS ) A4規格（210)^297公董） ------ (請先聞讀背面之注意事項再填寫本頁) 訂.1T -6- Printed by the Shellfish Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs _ __B7____ V. Description of the Invention (4) The device is composed of 5, 6, 7, 8, and false burner 9, and the exhaust of the rotary furnace 10 is false. The furnace 9 and the cyclone separators 8, 7, 6, and 5 are sequentially supplied. Thereafter, the cement raw material 1 ′ is put into the cyclone separator 5 in the uppermost stage, and the cement raw material L is heated at 8 50 ° C to 9 0 ° C until it reaches the cyclone separator 8 in the lower stage, and passes through the cement. Decarbonation of the limestone in the raw material L produces quicklime as follows. C a C〇3 ~ ^ C a 0 + C〇2 尙, the main component of the intermediate engineering product Q up to the lowermost cyclone 8, an example of which is S i〇2 19.0%, A 1 2 0 3 4.3%, F e 2 〇 3 2.7%, Ca 〇 60.5%, M g Ο 1. 1.5%, which are full of quicklime. In addition, the intermediate engineering product Q contains about 0.5% of unburned carbon. Thereafter, the intermediate process product Q containing quicklime is supplied to the rotary furnace 10 by the cyclone separator 8 at the lowest stage, and a tap valve 20 is provided at the exit below the cyclone separator 8 at the lowest stage. 2 0 and divide the designated amount of intermediate engineering products Q. Thereafter, the separated intermediate engineering product Q is passed through the water-cooled cooler 21, the conveyor 22, and out of the tank 24, and is transported to the sludge treatment plant of the sewage treatment facility via the transport vehicle 25. Alas, ′ 2 3 in FIG. 1 is an air plug feeder, and a dust collector is provided in the carrying-out tank 24. On the other hand, in the sludge treatment plant attached to the sewage treatment facility and the like, as shown in FIG. 2, the sewage sludge (dehydrated cake) s is dewatered by the dewatering device 3 1 and fed into the raw material mixer through the quantitative feeder 32. 4 〇. Alas, the sewage sludge S contains about 80% of water. In addition, in the cement containing quicklime, the paper size applies to the Chinese National Standard (CNS) A4 specification (210) ^ 297 public directors. ------ (Please read the precautions on the back before filling this page) Order
• m I HI 經濟部中央標準局貝工消費合作衽印製 A7 __________ 五、發明説明（5 ) 間工程品Q爲由搬送車2 5 ’通過原料槽2 6、輸送機 2 7、定量供給機2 8 ’以脫水材料型式投入原料混合機 4 0 〇 其後，於原料混合機4 0中’令下水污泥S與中間工 程品Q混合，且中間工程品Q中之生石灰成分與下水污泥 S中之水分爲如下反應，令下水污泥S中之水分於此水合 反應中消耗，或經由反應熱蒸發’而令下水污脫水。 CaO + HsO—Co (〇H) 2 如此處理令下水污泥3脫水’因使用來自水泥焙燒系 所分取之中間工程品Q作爲脫水材料，故比使用生石灰之 情形，可令下水污泥5較廉價地脫水’並且經由適度的反 應速度而可適當地脫水。又’因爲中間工程品Q爲微粉末 ，且含有少量的未燃燒碳’故可吸附下水污泥5中的臭氣 成分。 其後，下水污泥S之脫水後的固形成分Μ爲通過輸送 機4 1、乾燥粉粒貯藏槽4 3、輸送機4 3 ’並經由搬送 車2 5搬送至水泥工廠。其後’於水泥工廠中’如圖1所 示，脫水後之固形成分Μ爲由搬送車2 5 ’通過容納槽 4 5、輸送機4 6，並於水泥焙燒系之懸吊預熱器之最上 段的旋風分離器5中，與水泥原料L共同投入。 其次，以圖1、圖3及圖4說明脫水處理中使用可移 動脫水處理設備之第2實施形態。尙，關於與第一實施形 態同一部分爲使用同一符號並省略說明。 此脫水處理設備5 0爲如圖3、圖4所示，爲被固定 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） (請先閲讀背面之注意事項再填寫本頁) 'iT_ -8 - 10138° 五、發明説明（6) 地以卡車5 1搭載，並在此卡車5 1上進行脫水處理，於 卡車：5 1上搭載有將脫水材料中間工程品q投入收納之裝 脫水材料加料斗5 2、投入下水污泥S之裝污泥加料斗 53、由兩加料斗52、 53定量運送各材料之定量供給 機5 4、5 5 ’令來自該兩定量供給機所供給之中間工程 品Q與下水污泥S混合攪拌之原料混合機5 6、及將經由 此原料混合機5 6脫水處理後之固形成分予以排出之排出 運輸機5 7。 尙’於來自裝脫水材料加料斗5 2之定量供給機5 4 中爲使用螺旋運輸機，來自裝污泥加料斗之定量供給機 55及排出運輸機中爲使用帶式運輸機。 使用如此於卡車上搭載之脫水處理設備5 0，並分別 將來自污泥處理之脫水裝置所排出之下水污泥S，投入裝 下水污泥加料斗5 3，並將經由搬送車2 5運送之中間工 程品Q，投入裝脫水材料加料斗5 2中，且經由各定量供 給機5 4、5 5，以指定的混合比例分別供給，並由原料 混合機5 6之投入口 5 6 a被投入。 其後，於原料混合機5 6中，令下水污泥S與中間工 程品Q混合，且中間工程品Q中之生石灰成分與下水污泥 S中之水分爲與前述同樣地反應，使下水污泥S中之水分 於此水合反應中消耗，或經由反應熱蒸發，而令下水污泥 S脫水。 其後，下水污泥S之脫水後的固形成分Μ爲與實施形 態1相同，經由搬送車2 5搬送至水泥工廠’並於水泥工 本紙張尺度適用中國國家標準（CNS ) Α4規格（210X297公釐） (請先閱讀背面之注意事項再填寫本頁) 訂 經濟部中央標準局員工消費合作社印製 -9- 經濟部中央標準局員工消費合作社印製 A7 ____ B7 五、發明説明（7 ) 廠中，如圖3所示，通過容納槽45、輸送機46，並於 水泥焙燒系之懸吊預熱器之最上段的旋風分離器5中，與 水泥原料共同投入。 如上述，第1、第2實施形態雖均爲令下水污泥S之 脫水後的固形成分Μ與水泥原料L共同投入，但因使用由 水泥焙燒系所分取之中間工程品Q作爲脫水材料，故，可 令下水污泥Q之脫水後的固形成分Μ就其原樣的水泥原料 L共同投入，不會令水泥製品之性能降低，並可適當處理 固形成分Μ。 尙，上述兩實施形態雖敘述關於水泥焙燒系之懸吊預 熱器具備假燒爐之情形，但並非一定必須具備假燒爐。又 ，上述兩實施形態敘述關於由水泥焙燒系之懸吊預熱器之 最下段旋風分離器分取中間工程品之情形，但由中段之旋 風分離器分取亦可。 於上述各實施形態中雖敘述關於下水處理設施所發生 之下水污泥的處理，但本發明亦可用樣地實施於其他屎尿 處理設施所發生之水分含量爲6 0〜8 0%之屎尿污泥之 處理。 又，由於在屎尿污泥及下水污泥中，含有許多氨成分 ，故若將脫水後之固形成分與水泥材料共同焙燒，則在焙 燒系內發生許多氨氣，且有降低排氣中氮氣化物濃度之效 果。 〔發明之效果〕 本紙張尺度適用中國國家標準（CNS ) Α4規格（210X297公釐） (諳先閱讀背面之注意事項再填寫本頁)• m I HI Printed A7 by the shellfish consumer cooperation of the Central Bureau of Standards of the Ministry of Economic Affairs __________ 5. Description of the invention (5) The engineering product Q is transported by the transport vehicle 2 5 'through the raw material tank 2 6. Conveyor 2 7. Quantitative feeder 2 'Into the raw material mixer 400 as a dewatering material type, and then in the raw material mixer 40', the sewage sludge S is mixed with the intermediate engineering product Q, and the quicklime component in the intermediate engineering product Q and the sewage sludge are mixed. The water in S is the following reaction, so that the water in the sewage sludge S is consumed in this hydration reaction, or the sewage is dehydrated through the reaction heat evaporation. CaO + HsO—Co (〇H) 2 is treated in this way to dewater the sewage sludge 3 'because the intermediate engineering product Q from the cement roasting system is used as a dehydration material, so the sewage sludge 5 can be made more than when using quicklime It is cheaper to dehydrate 'and can be properly dehydrated via a moderate reaction speed. Since the intermediate engineering product Q is fine powder and contains a small amount of unburned carbon, it can adsorb odor components in the sewage sludge 5. After that, the dewatered sludge S has a solid fraction M that is transported to a cement plant via a conveyor 41, a dry powder storage tank 4 3, and a conveyor 4 3 'via a transport vehicle 25. Thereafter, in the cement plant, as shown in FIG. 1, the dehydrated solid component M is transported by the transport vehicle 2 5 'through the storage tank 4 5 and the conveyor 4 6, and suspended in the preheater of the cement roasting system. The uppermost cyclone separator 5 is fed together with the cement raw material L. Next, a second embodiment in which a mobile dehydration treatment device is used in the dehydration treatment will be described with reference to Figs. 1, 3, and 4. Alas, the same reference numerals are used for the same parts as those in the first embodiment, and the description is omitted. This dewatering equipment 50 is shown in Figures 3 and 4, and is fixed to the paper size. The Chinese National Standard (CNS) A4 specification (210X297 mm) is applied (please read the precautions on the back before filling this page) '' iT_ -8-10138 ° 5. Description of the invention (6) The truck 51 is mounted on the truck 51, and the truck 51 is dehydrated. The truck: 51 is equipped with a device for putting the dewatering material intermediate engineering product q into the storage. Dewatering material charging hopper 5 2. The sludge charging hopper 53 for loading the sewage sludge S, and the quantitative feeding machines 5 and 5 5 for quantitatively transporting each material from the two feeding hoppers 52 and 53. A raw material mixer 56 that mixes and stirs the intermediate engineering product Q and the sewage sludge S, and a discharge conveyor 57 that discharges the solid components after the dehydration treatment by this raw material mixer 56. For the quantitative feeder 5 4 from the dehydrating material charging hopper 5 2, a screw conveyor is used. For the quantitative feeder 55 from the sludge loading hopper and the discharge conveyor, a belt conveyor is used. The dewatering treatment equipment 50 installed on the truck is used, and the lower water sludge S discharged from the sludge treatment dewatering device is respectively put into the water sludge charging hopper 5 3 and transported by the transport vehicle 25. The intermediate engineering product Q is put into the dewatering material charging hopper 5 2 and is supplied through the quantitative feeders 5 4 and 5 5 at a specified mixing ratio, and is input through the inlet 5 6 a of the raw material mixer 5 6. . Thereafter, in the raw material mixer 56, the sewage sludge S is mixed with the intermediate engineering product Q, and the quicklime component in the intermediate engineering product Q and the moisture in the sewage sludge S are reacted in the same manner as described above to make the sewage sewage The water in the sludge S is consumed in the hydration reaction, or the sewage sludge S is dehydrated by the heat of reaction. Thereafter, the solid content M of the sewage sludge S after dehydration is the same as that in Embodiment 1, and is transported to the cement factory through a transport vehicle 25, and the Chinese National Standard (CNS) A4 specification (210X297 mm) is applied to the paper size of the cement. ) (Please read the notes on the back before filling out this page) Order printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs -9- Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs A7 ____ B7 V. Description of Invention (7) In the factory As shown in FIG. 3, through the storage tank 45, the conveyor 46, and the cyclone separator 5 in the uppermost stage of the suspension preheater of the cement roasting system, it is jointly input with the cement raw materials. As described above, although the first and second embodiments both jointly input the solid content M after the dewatering of the sewage sludge S and the cement raw material L, the intermediate engineering product Q separated by the cement roasting system is used as the dewatering material. Therefore, the dewatered sludge Q can be co-injected with its original cement raw material L, which will not reduce the performance of the cement product, and can properly treat the solid formed component M. Alas, although the above two embodiments describe the case where the suspension preheater of the cement roasting system is provided with a false burner, it is not necessary to have a false burner. In the above two embodiments, the case where the middle stage cyclone separator is used to separate intermediate cement products from the cement pre-heating suspension preheater is described, but the middle stage cyclone separator may be used to separate the intermediate engineering products. Although the above embodiments describe the treatment of the sewage sludge generated in the sewage treatment facility, the present invention can also be applied to the fecal urine sludge having a moisture content of 60 to 80% in other feces treatment facilities. Its processing. In addition, since fecal urine sludge and sewage sludge contain a lot of ammonia components, if the dehydrated solid content is co-fired with the cement material, a lot of ammonia gas will be generated in the roasting system, and the nitrogen compounds in the exhaust gas will be reduced. The effect of concentration. [Effects of the invention] This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) (谙 Please read the precautions on the back before filling in this page)
-10 - 經濟部中央標準局員工消费合作社印聚 A7 B7五、發明説明（8 ) 如上述，本發明之下水污泥的處理方法爲經由令加熱 水泥原料所得之含有生石灰的中間工程品，由水泥焙燒系 之懸吊預熱器中分取，並作爲脫水材料於含有機質污泥中 混合且脫水，而含有機質污泥之脫水後的固形成分，因爲 於焙燒後以固形成分型式殘留之成分爲接近水泥原料，故 即使將前述脫水後之固形成分就其原樣使用作爲水泥原料 ，亦不會令所製造之水泥品質變化，可將含有機質污泥經 濟且有效率地處理。又，使用作爲脫水材料之來自水泥培 燒系所分取之中間工程品爲微粉末，且因含有少量的未燃 燒碳，故於含有機質污泥之脫臭上亦具效果。 再者，經由令脫水處理設備於卡車上固定搭載，使其 可能移動，使得多數的中小規模含有機質處理設施中可輕 易共同一個脫水處理設備，使設備之運轉率提高，並且可 削減處理費用。 〔圖面之簡單說明〕 〔圖1〕示出本發明之含有機質污泥處理方法之第1 實施形態之於水泥工廠中之作業槪略圖。 〔圖2〕示出同上之污泥處理場中之作業槪略圖。 〔圖3〕示出本發明之含有機質污泥處理方法之第2 實施形態之污泥處理設備中之作業槪略圖。 〔圖4〕將同上之脫水處理設備於卡車上搭載狀態之 一例的側面圖。 (請先閲讀背面之注意事項再填寫本頁) -訂 本紙張尺度適用中國國家標準（CNS ) A4規格（210 X 297公釐） -11 - ιίί 五、發明説明（9 ) 〔符號之說明〕 1 原料貯藏場 2 原料乾燥機 3 原料粉碎機 4 原料槽 5、6、7、8 旋風分離器（懸吊預熱器） 9 假燒爐 1 0 旋轉爐 2 0 分取槽 2 1 冷卻機 2 2 輸送機 2 3 氣塞加料器 2 4 運出槽 2 5 搬送車 2 6 原料槽 2 7 輸送機 2 8 定量供給機 3 1 污泥脫水裝置 3 2 定量供給機 4 0 原料混合機 4 1 輸送機 4 2 乾燥粉粒子體貯藏槽 4 3 輸送機 4 4 搬送車 經濟部中央標準局員工消費合作社印製 (讀先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） -12- A7 B7 五、發明説明（1〇) 4 5 容納槽 4 6 輸送機 5 0 脫水處理設備 5 1 卡車 5 2 裝脫水材料加料斗 5 3 裝含有機質污泥加料斗 5 4、 55 定量供給機 5 6 原料混合機 5 7 排出運輸機 L 水泥原料 Μ 含有機質污泥脫水後之固形成分 Q 水泥中間工程品 S 下水污泥 (請先閱讀背面之注意事項再填寫本頁)-10-Yinju A7, B7, Consumer Cooperatives, Central Standards Bureau, Ministry of Economic Affairs, A7 B7 V. Description of Invention (8) As mentioned above, the water sludge treatment method according to the present invention is an intermediate engineering product containing quicklime obtained by heating cement raw materials. It is taken from the suspension preheater of the cement roasting system, and is mixed and dehydrated in organic sludge as a dewatering material, and the solid content after dehydration of the organic sludge is because the components remaining in solid form after baking are solid components. In order to be close to the cement raw material, even if the aforementioned dehydrated solid content is used as it is as a cement raw material, the quality of the manufactured cement will not be changed, and the organic-containing sludge can be processed economically and efficiently. In addition, the intermediate engineering product collected from the cement firing system as a dewatering material is fine powder and contains a small amount of unburned carbon, so it is also effective in deodorizing organic sludge. In addition, the dehydration treatment equipment is fixedly mounted on the truck to make it possible to move, so that most of the small and medium-sized organic-containing processing facilities can easily share a dehydration treatment equipment, which can improve the operation rate of the equipment and reduce the processing cost. [Brief Description of Drawings] [Figure 1] A schematic diagram showing the operation in a cement plant of the first embodiment of the organic sludge treatment method according to the present invention. [Fig. 2] A schematic diagram of the operation in the sludge treatment plant as described above. [Fig. 3] A schematic diagram showing an operation in a sludge treatment facility according to a second embodiment of the organic sludge treatment method according to the present invention. [Fig. 4] A side view showing an example of a state where the dehydration treatment equipment is mounted on a truck. (Please read the precautions on the back before filling this page)-The size of the paper used for this edition applies to the Chinese National Standard (CNS) A4 (210 X 297 mm) -11-ιίί 5. Description of the invention (9) [Explanation of symbols] 1 Raw material storage site 2 Raw material dryer 3 Raw material pulverizer 4 Raw material tanks 5, 6, 7, 8 Cyclone separator (suspension preheater) 9 Fake furnace 1 0 Rotary furnace 2 0 Dispenser 2 1 Cooler 2 2 Conveyor 2 3 Air plug feeder 2 4 Out of tank 2 5 Transport vehicle 2 6 Raw material tank 2 7 Conveyor 2 8 Dosing feeder 3 1 Sludge dewatering device 3 2 Dosing feeder 4 0 Raw material mixer 4 1 Conveying Machine 4 2 Dry powder granule storage tank 4 3 Conveyor 4 4 Transport truck Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs (read the precautions on the back before filling out this page) This paper size applies to Chinese National Standards (CNS) A4 specification (210X297 mm) -12- A7 B7 V. Description of the invention (10) 4 5 Containing tank 4 6 Conveyor 5 0 Dewatering equipment 5 1 Truck 5 2 Loading dewatering material hopper 5 3 Loading organic sludge Hopper 5 4, 55 Dosing The mixer 56 the raw material discharge conveyor 57 L of cement material Μ solid component S Q cement intermediate product engineering sewage sludge containing organic matter sludge dewatering (Read Notes on the back and then fill the page)
1T 經濟部中央標準局員工消費合作社印製 本紙張尺度適用中國國家標準（CNS ) Α4規格（210Χ297公釐） -13-1T Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs This paper is sized to the Chinese National Standard (CNS) Α4 (210 × 297 mm) -13-