CN103301715A - Method for supplying adsorbent to fluidized floating bed and purification system using the same - Google Patents

Abstract

The invention relates to a method for supplying an adsorption material of a fluidized floating bed and a purification system using the method, wherein the method is characterized in that the adsorption material with adsorption capacity is stored in advance, and the position where the adsorption material is stored in advance is higher than an adsorption material inlet of the fluidized floating bed, so that the adsorption material stored in advance is rapidly distributed in the fluidized floating bed by utilizing gravity potential energy; however, the adsorption material stored in advance is accumulated by intercepting the adsorption material which is originally excessively supplied during the operation of the fluidized floating bed, or is accumulated by using the original adsorption material supply mechanism when the fluidized floating bed is not operated. Therefore, the problem that the adsorption material cannot be rapidly supplied in the prior art is solved, and the adsorption material can be rapidly supplied.

Description

Translated fromChinese

流体化浮动床的吸附材供给方法及使用该方法的净化系统Adsorbent material supply method for fluidized floating bed and purification system using same

技术领域technical field

本发明是有关一种流体化浮动床的吸附材供给方法及使用该方法的净化系统，尤指种将具有吸附能力的吸附材预先贮存高于流体化浮动床吸附材进入口的位置，以利用重力位能而快速分布于流体化浮动床的设计。The invention relates to a method for supplying an adsorbent material of a fluidized floating bed and a purification system using the method, in particular to pre-storing the adsorbent material with adsorption capacity at a position higher than the inlet of the adsorbent material of the fluidized floating bed to utilize Gravitational potential can be rapidly distributed in a fluidized floating bed design.

背景技术Background technique

如图1所示，现有的流体化浮动床净化系统，其令待处理废气以废气风机13送入流体化浮动床10的底部，废气气流借气流分散板12分散后，与由上落下的吸附材30接触，即可成为净化气体并从塔顶排放；其中，流体化浮动床10的内部以多孔板11分隔成数层，吸附材30由流体化浮动床10顶端的吸附材进入口15落下，而在多孔板11的上方形成浮动层，并沿着多孔板11一层一层的开口部落下，当吸附材30与含有机化合物的废气接触时，将废气中的有机化合物吸附于吸附材30的孔洞内，废气即变成净化气体排放。As shown in Figure 1, the existing fluidized floating bed purification system makes the waste gas to be treated be sent to the bottom of the fluidized floatingbed 10 with thewaste gas blower 13, and after the waste gas flow is dispersed by the airflow dispersion plate 12, it is combined with the falling from the top When the adsorbent 30 contacts, it becomes a purified gas and is discharged from the top of the tower; wherein, the inside of the fluidizedfloating bed 10 is divided into several layers by theporous plate 11, and the adsorbent 30 enters theinlet 15 from the adsorbent at the top of the fluidized floatingbed 10 Fall, and form a floating layer above theporous plate 11, and fall along the openings of theporous plate 11 layer by layer, when theadsorption material 30 contacts with the waste gas containing organic compounds, the organic compounds in the waste gas are adsorbed on the adsorption In the holes of thematerial 30, the exhaust gas becomes purified gas and discharged.

再者，当吸附材30落至流体化浮动床10底部的贮槽14后，借吸附材输送装置20的输送气源22，以待脱附气源管232与已脱附气源管272送出空气或氮气形成推送力，经吸附出料管21、待脱附下输送槽23、待脱附输送管231、待脱附上输送槽24与脱附进料管25送至脱附塔40的顶端，进行脱附再生的工作；脱附再生后的吸附材30则以脱附出料管26、已脱附下输送槽27、已脱附输送管271、已脱附上输送槽28与吸附进料管29送回流体化浮动床10顶端的吸附材进入口15。Furthermore, when the adsorbent 30 falls to thestorage tank 14 at the bottom of the fluidizedfloating bed 10, thegas source 22 of theadsorbent conveying device 20 is used to send out the desorbedgas source pipe 232 and the desorbedgas source pipe 272. Air or nitrogen forms a pushing force, and is sent to thedesorption tower 40 through theadsorption discharge pipe 21, thelower conveying tank 23 to be desorbed, the conveyingpipe 231 to be desorbed, theupper conveying tank 24 to be desorbed, and thedesorption feed pipe 25. At the top, the work of desorption and regeneration is carried out; theadsorbent material 30 after desorption and regeneration is desorbed with thedischarge pipe 26, the desorbedlower conveying tank 27, thedesorbed conveying pipe 271, the desorbedupper conveying groove 28 and the adsorption Thefeed pipe 29 is sent back to theinlet 15 of the adsorbent at the top of the fluidizedfloating bed 10 .

此外，待再生的吸附材30在脱附塔40慢慢往下流动，并经由脱附热源42加热，再由脱附塔40下方的脱附气源43吹入氮气与吸附材30接触，将吸附材30中的有机化合物脱附，且将脱附气流输出管41连结至后续的诸如冷凝器的净化装置50；其中，经加热脱附后的吸附材30再经脱附塔40底部冷却后，由前述的输送过程送回流体化浮动床10，再度吸收有机化合物。In addition, the adsorbent 30 to be regenerated slowly flows downward in thedesorption tower 40, and is heated by thedesorption heat source 42, and then nitrogen gas is blown into the desorption gas source 43 below thedesorption tower 40 to contact the adsorbent 30, and the The organic compound in theadsorption material 30 is desorbed, and the desorption gasflow output pipe 41 is connected to thesubsequent purification device 50 such as a condenser; wherein, theadsorption material 30 after heating and desorption is cooled by the bottom of thedesorption tower 40 , sent back to the fluidized floatingbed 10 by the aforementioned conveying process to absorb organic compounds again.

然而，当流体化浮动床净化系统停止运转时，原本浮动于各该多孔板11上方的吸附材30，会全部落至该流体化浮动床10底部的贮槽14，故当流体化浮动床净化系统重新开机运转时，必须借由前述的输送过程将吸附材30送回流体化浮动床10，等到吸附材30重新布满于各该多孔板11上方，才可将待处理废气导入该流体化浮动床10进行净化；不过，由于等待吸附材30重新布满于各该多孔板11上方所耗费的时间甚长(可能约需2小时)，对于必须频繁停机与开机的使用者而言，不甚方便。又，虽然流体化浮动床10原本有超额供给吸附材30的设计，但当有突发性高浓度待处理废气必须处理且超过处理能力的上限时，流体化浮动床10原有的吸附材供给机制，并无法快速供给吸附材以弥补不足的处理能力。However, when the fluidized floating bed purification system stopped running, theadsorbent material 30 originally floating on each of theperforated plates 11 would all fall to thestorage tank 14 at the bottom of the fluidized floatingbed 10, so when the fluidized floating bed is purified When the system is restarted, theadsorption material 30 must be sent back to the fluidized floatingbed 10 through the aforementioned conveying process, and the waste gas to be treated can only be introduced into the fluidized floatingbed 10 after theadsorption material 30 is refilled above theporous plates 11. The floatingbed 10 is used for purification; however, because it takes a long time (maybe about 2 hours) to wait for the adsorbent 30 to refill on each of theporous plates 11, it is not recommended for users who must frequently stop and start Very convenient. Also, although the fluidized floatingbed 10 originally had an excess supply design for the adsorbent 30, when there is a sudden high concentration of waste gas to be treated that must be treated and exceeds the upper limit of the processing capacity, the original adsorbent supply of the fluidized floatingbed 10 mechanism, and cannot quickly supply adsorbents to make up for insufficient processing capacity.

发明内容Contents of the invention

为解决先前技术无法快速供给吸附材的问题，本发明提供一种流体化浮动床的吸附材供给方法及使用该方法的净化系统，其具有快速供给吸附材的功效。In order to solve the problem that the prior art cannot quickly supply adsorbents, the present invention provides a method for supplying adsorbents in a fluidized floating bed and a purification system using the method, which has the effect of rapidly supplying adsorbents.

本发明解决其技术问题所采用的技术方案是：The technical solution adopted by the present invention to solve its technical problems is:

本发明的流体化浮动床的吸附材供给方法，是将具有吸附能力的吸附材预先贮存，且令吸附材预先贮存的位置高于流体化浮动床的吸附材进入口，使预先贮存的吸附材利用重力位能而快速分布于流体化浮动床者。其中，预先贮存的吸附材于流体化浮动床运转过程中，截取原本所超额供给的吸附材而累积贮存；或者，预先贮存的吸附材于流体化浮动床未运转之际，利用原有的吸附材供给机制而累积贮存。The adsorption material supply method of the fluidized floating bed of the present invention is to pre-store the adsorption material with adsorption capacity, and make the position where the adsorption material is stored in advance higher than the inlet of the adsorption material of the fluidized floating bed, so that the pre-stored adsorption material Those who quickly distribute in the fluidized floating bed by using the gravitational potential energy. Among them, during the operation of the fluidized floating bed, the pre-stored adsorbent intercepts the excess adsorbent and accumulates it; or, when the fluidized floating bed is not in operation, the pre-stored adsorbent uses the original adsorbent Accumulated storage by the material supply mechanism.

此外，本发明使用前述方法的流体化浮动床净化系统第一实施例，包括有：一流体化浮动床，让吸附材由顶端的吸附材进入口导入并沿着数个多孔板逐层落至底部，而吸附待处理废气中的有机化合物；一脱附塔，让吸附材由顶端落至底部而将所吸附的有机化合物加热脱附；一吸附材输送装置，将落至该流体化浮动床底部的吸附材输送至该脱附塔顶端，且将落至该脱附塔底部的吸附材输送至该流体化浮动床顶端的吸附材进入口；以及一快速供料贮槽，设置于该吸附材输送装置用以连结至该吸附材进入口的吸附进料管，且设置有吸附材供料流量控制阀。In addition, the first embodiment of the fluidized floating bed purification system using the aforementioned method of the present invention includes: a fluidized floating bed, allowing the adsorbent to be introduced from the inlet of the adsorbent at the top and fall down layer by layer along several porous plates. The bottom is used to adsorb the organic compounds in the waste gas to be treated; a desorption tower allows the adsorbent to fall from the top to the bottom to heat and desorb the adsorbed organic compounds; a conveying device for the adsorbent will fall to the fluidized floating bed The adsorption material at the bottom is transported to the top of the desorption tower, and the adsorption material falling to the bottom of the desorption tower is transported to the inlet of the adsorption material at the top of the fluidized floating bed; and a fast feeding storage tank is arranged on the adsorption The material conveying device is used to connect to the adsorption feed pipe of the adsorption material inlet, and is provided with an adsorption material feed flow control valve.

然而，该吸附材输送装置包括有：输送气源、待脱附下输送槽、待脱附上输送槽、已脱附下输送槽、已脱附上输送槽、连结该流体化浮动床底部与待脱附下输送槽的吸附出料管、连结待脱附下输送槽与待脱附上输送槽的待脱附输送管、连结待脱附上输送槽与该脱附塔顶端的脱附进料管、连结该脱附塔底部与已脱附下输送槽的脱附出料管、连结已脱附下输送槽与已脱附上输送槽的已脱附输送管、连结已脱附上输送槽与该吸附材进入口的吸附进料管、连结该输送气源与待脱附下输送槽的待脱附气源管以及连结该输送气源与已脱附下输送槽的已脱附气源管。又，该流量控制阀于流体化浮动床运转过程中，控制吸附材供料流量用以截取超额供给的吸附材，进而累积贮存于该快速供料贮槽内。另，该流量控制阀于流体化浮动床未运转的际完全关闭，而借该吸附材输送装置输送吸附材累积贮存于该快速供料贮槽内。However, the adsorbent delivery device includes: a delivery gas source, a lower delivery tank to be desorbed, an upper delivery tank to be desorbed, a lower delivery tank that has been desorbed, an upper delivery tank that has been desorbed, and a connection between the bottom of the fluidized floating bed and the The adsorption discharge pipe of the lower conveying tank to be desorbed, the desorbed conveying pipe connecting the lower conveying tank to be desorbed and the upper conveying tank to be desorbed, the desorption inlet connecting the upper conveying tank to be desorbed and the top of the desorption tower Material pipe, the desorption discharge pipe connecting the bottom of the desorption tower with the desorbed lower conveying tank, the desorbed conveying pipe connecting the desorbed lower conveying tank and the desorbed upper conveying tank, and the desorbed upper conveying pipe The adsorption feed pipe of the tank and the inlet of the adsorbent material, the gas source pipe to be desorbed that connects the delivery gas source and the lower delivery tank to be desorbed, and the desorbed gas that connects the delivery gas source and the lower delivery tank that has been desorbed source pipe. In addition, the flow control valve controls the feed flow rate of the adsorbent material during the operation of the fluidized floating bed to intercept the excess adsorbent material, and then accumulate and store it in the fast feed storage tank. In addition, the flow control valve is completely closed when the fluidized floating bed is not in operation, and the adsorbent conveying device is used to transport the adsorbent to be accumulated and stored in the fast feeding storage tank.

再者，本发明使用前述方法的流体化浮动床净化系统第二实施例，包括有：一流体化浮动床，让吸附材由顶端的吸附材进入口导入并沿着数个多孔板逐层落至底部，而吸附待处理废气中的有机化合物；一脱附塔，让吸附材由顶端落至底部而将所吸附的有机化合物加热脱附；以及一吸附材输送装置，将落至该流体化浮动床底部的吸附材输送至该脱附塔顶端，且将落至该脱附塔底部的吸附材输送至该流体化浮动床顶端的吸附材进入口，而包括有：输送气源、待脱附下输送槽、待脱附上输送槽、已脱附下输送槽、快速供料贮槽、连结该流体化浮动床底部与待脱附下输送槽的吸附出料管、连结待脱附下输送槽与待脱附上输送槽的待脱附输送管、连结待脱附上输送槽与该脱附塔顶端的脱附进料管、连结该脱附塔底部与已脱附下输送槽的脱附出料管、连结已脱附下输送槽与快速供料贮槽的已脱附输送管、连结快速供料贮槽与该吸附材进入口的吸附进料管、连结该输送气源与待脱附下输送槽的待脱附气源管以及连结该输送气源与已脱附下输送槽的已脱附气源管；然而，进一步令该已脱附输送管伸入该已脱附上输送槽内部，且于该吸附进料管设置有吸附材供料流量控制阀。Furthermore, the second embodiment of the fluidized floating bed purification system using the aforementioned method of the present invention includes: a fluidized floating bed, allowing the adsorbent to be introduced from the inlet of the adsorbent at the top and fall layer by layer along several porous plates to the bottom, and adsorb the organic compounds in the waste gas to be treated; a desorption tower, which allows the adsorbent to fall from the top to the bottom to heat and desorb the adsorbed organic compounds; and a conveying device for the adsorbent, which will fall to the fluidized The adsorbent material at the bottom of the floating bed is transported to the top of the desorption tower, and the adsorbent material falling to the bottom of the desorption tower is transported to the inlet of the adsorbent material at the top of the fluidized floating bed, which includes: transport gas source, to-be-desorbed Attached lower delivery tank, upper delivery tank to be desorbed, lower delivery tank that has been desorbed, fast feeding storage tank, adsorption discharge pipe connecting the bottom of the fluidized floating bed with the lower delivery tank to be desorbed, and connected to the lower delivery tank to be desorbed The delivery tank and the delivery pipe to be desorbed to the upper delivery tank to be desorbed, the desorption feed pipe connecting the upper delivery tank to be desorbed and the top of the desorption tower, and the desorption feed pipe connecting the bottom of the desorption tower to the lower delivery tank that has been desorbed The desorption discharge pipe, the desorbed conveying pipe connecting the desorbed lower conveying tank and the fast feeding storage tank, the adsorption feeding pipe connecting the fast feeding storage tank and the inlet of the adsorbent, connecting the conveying gas source and the The gas source pipe to be desorbed in the lower delivery tank to be desorbed and the desorbed gas source tube connecting the delivery gas source and the lower delivery tank; however, the desorbed delivery tube is further extended into the desorbed Inside the upper delivery tank, an adsorption material feed flow control valve is arranged on the adsorption feed pipe.

另者，该流量控制阀于流体化浮动床运转过程中，控制吸附材供料流量用以截取超额供给的吸附材，进而累积贮存于该快速供料贮槽内。又，该流量控制阀于流体化浮动床未运转的际完全关闭，而借该吸附材输送装置输送吸附材累积贮存于该快速供料贮槽内。In addition, during the operation of the fluidized floating bed, the flow control valve controls the feed flow rate of the adsorbent material so as to intercept the oversupplied adsorbent material, and then accumulate and store it in the fast feed storage tank. In addition, the flow control valve is completely closed when the fluidized floating bed is not in operation, and the adsorbents are transported and stored in the fast feeding storage tank by the adsorbent conveying device.

本发明的有益效果是，其具有快速供给吸附材的功效。The beneficial effect of the present invention is that it has the effect of rapidly supplying the adsorbent.

附图说明Description of drawings

下面结合附图和实施例对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.

图1是现有流体化浮动床净化系统的结构示意图。Figure 1 is a schematic structural view of an existing fluidized floating bed purification system.

图2是本发明第一实施例的结构示意图。Fig. 2 is a schematic structural diagram of the first embodiment of the present invention.

图3是本发明第二实施例的结构示意图。Fig. 3 is a schematic structural diagram of the second embodiment of the present invention.

图中标号说明：Explanation of symbols in the figure:

10流体化浮动床10 fluidized floating bed

11多孔板11 multi-well plate

12气流分散板12 air distribution plate

13废气风机13 exhaust fan

14贮槽14 storage tanks

15吸附材进入口15 Adsorption material inlet

20吸附材输送装置20 Adsorbent conveying device

21吸附出料管21 Adsorption discharge pipe

22输送气源22 delivery gas source

23待脱附下输送槽23 The lower delivery tank to be desorbed

231待脱附输送管231 Delivery pipe to be desorbed

232待脱附气源管232 Gas source pipe to be desorbed

24待脱附上输送槽24 to be desorbed on the delivery tank

25脱附进料管25 desorption feed tube

26脱附出料管26 desorption discharge pipe

27已脱附下输送槽27 has been desorbed lower delivery tank

271、271a已脱附输送管271, 271a desorbed delivery pipe

272已脱附气源管272 desorbed gas source tube

28、28a已脱附上输送槽28, 28a have been desorbed from the upper conveying trough

29吸附进料管29 adsorption feed pipe

30吸附材30 Adsorbent

40脱附塔40 desorption tower

41脱附气流输出管41 desorption gas output pipe

42脱附热源42 desorption heat source

43脱附气源43 desorption gas source

50净化装置50 purification device

60快速供料贮槽60 fast feed storage tank

61流量控制阀61 flow control valve

具体实施方式Detailed ways

首先，请参阅图2所示，本发明是用以流体化浮动床的吸附材供给净化系统的流体化浮动床，而该流体化浮动床净化系统包括有：一流体化浮动床10，让吸附材30由顶端的吸附材进入口15导入并沿着数个多孔板11逐层落至底部的贮槽14，而吸附待处理废气中的有机化合物；一脱附塔40，让吸附材30由顶端落至底部而将所吸附的有机化合物加热脱附；以及一吸附材输送装置20，将落至该流体化浮动床10底部的吸附材30经待脱附下输送槽23与待脱附上输送槽24输送至该脱附塔40顶端，且将落至该脱附塔40底部的吸附材30经已脱附下输送槽27与已脱附上输送槽28输送至该流体化浮动床10顶端的吸附材进入口15。At first, please refer to shown in Fig. 2, the present invention is to supply the fluidized floating bed of the adsorption material of the fluidized floating bed purification system, and the fluidized floating bed purification system includes: a fluidized floatingbed 10, allowing the adsorption Thematerial 30 is introduced from theadsorption material inlet 15 at the top and falls to thestorage tank 14 at the bottom layer by layer along severalporous plates 11 to adsorb organic compounds in the waste gas to be treated; adesorption tower 40 allows theadsorption material 30 to The top falls to the bottom to heat and desorb the adsorbed organic compound; and anadsorbent conveying device 20, the adsorbent 30 that falls to the bottom of the fluidizedfloating bed 10 passes through thelower delivery tank 23 to be desorbed and the upper to be desorbed Thetransport tank 24 is transported to the top of thedesorption tower 40, and the adsorbent 30 that has fallen to the bottom of thedesorption tower 40 is transported to the fluidized floatingbed 10 through the desorbedlower transport tank 27 and the desorbedupper transport tank 28. Adsorbent material at the top entersport 15 .

再者，该吸附材输送装置20系包括有：输送气源22、待脱附下输送槽23、待脱附上输送输24、已脱附下输送槽27、已脱附上输送槽28、连结该流体化浮动床10底部与待脱附下输送槽23的吸附出料管21、连结待脱附下输送槽23与待脱附上输送槽24的待脱附输送管231、连结待脱附上输送槽24与该脱附塔40顶端的脱附进料管25、连结该脱附塔40底部与已脱附下输送槽27的脱附出料管26、连结已脱附下输送槽27与已脱附上输送槽28的已脱附输送管271、连结已脱附上输送槽28与该吸附材进入口15的吸附进料管29、连结该输送气源22与待脱附下输送槽23的待脱附气源管232以及连结该输送气源22与已脱附下输送槽27的已脱附气源管272。Furthermore, the adsorptionmaterial delivery device 20 includes: adelivery gas source 22, alower delivery tank 23 to be desorbed, anupper delivery tank 24 to be desorbed, alower delivery tank 27 that has been desorbed, anupper delivery tank 28 that has been desorbed, Theadsorption discharge pipe 21 connecting the bottom of the fluidized floatingbed 10 with thelower delivery tank 23 to be desorbed, thedelivery tube 231 to be desorbed connected to thelower delivery tank 23 to be desorbed and theupper delivery tank 24 to be desorbed, and thedelivery tube 231 to be desorbedAttach delivery tank 24 and thedesorption feed pipe 25 at the top of thedesorption tower 40, connect the bottom of thedesorption tower 40 with thedesorption discharge pipe 26 of the desorptionlower delivery tank 27, connect the desorptionlower delivery tank 27 and thedesorbed conveying pipe 271 of the desorbedupper conveying tank 28, theadsorption feeding pipe 29 connecting the desorbedupper conveying tank 28 and theinlet 15 of the adsorbent, connecting theconveying gas source 22 and the lower Thegas source pipe 232 to be desorbed in theconveying tank 23 and the desorbedgas source pipe 272 connecting theconveying gas source 22 and the desorbedlower conveying tank 27 .

然而，本发明的吸附材供料装置的第一实施例，进一步设置一快速供料贮槽60于该吸附材输送装置20用以连结至该吸附材进入口15的吸附进料管29，且于该吸附进料管29设置有吸附材供料流量控制阀61。However, in the first embodiment of the adsorption material feeding device of the present invention, a fastfeeding storage tank 60 is further arranged on the adsorptionmaterial conveying device 20 to be connected to theadsorption feeding pipe 29 of theadsorption material inlet 15, and Theadsorption feed pipe 29 is provided with an adsorption material supplyflow control valve 61 .

另者，请参阅图3所示，本发明的吸附材供料装置的第二实施例，进一步令该已脱附输送管271a伸入该已脱附上输送槽28a内部，而致使该已脱附上输送槽28a内部低于该已脱附输送管271a顶端的空间成为让吸附材累积贮存的空间(已脱附上输送槽28a较一般的已脱附上输送槽28加大其内部空间)，俾使累积贮存的吸附材得以用于快速供料，且于该吸附进料管29设置有吸附材供料流量控制阀61。In addition, please refer to Fig. 3, the second embodiment of the adsorption material feeding device of the present invention further makes the desorbed conveyingpipe 271a extend into the desorbedupper conveying tank 28a, so that the desorbed The space inside the attacheddelivery tank 28a that is lower than the top of the desorbeddelivery tube 271a becomes a space for the accumulation and storage of adsorbents (the desorbedupper delivery tank 28a has a larger internal space than the general desorbed upper delivery tank 28) , so that the accumulated and stored adsorbents can be used for rapid feeding, and theadsorbent feeding pipe 29 is provided with an adsorbent feedflow control valve 61 .

基于上述的构成，本发明是将具有吸附能力的吸附材预先贮存于前述第一实施例的快速供料贮槽60或是第二实施例的已脱附上输送槽28a，而由于此等让吸附材30预先贮存的位置必然会高于流体化浮动床10的吸附材进入口15，可让预先贮存的吸附材30利用重力位能而快速分布于流体化浮动床30内部的各该多孔板11。Based on the above-mentioned constitution, the present invention pre-stores the adsorbent material with adsorption capacity in the fastfeeding storage tank 60 of the aforementioned first embodiment or the desorbedupper conveying tank 28a of the second embodiment, and because these allow The pre-stored position of the adsorbent 30 must be higher than theinlet 15 of the adsorbent of the fluidized floatingbed 10, so that thepre-stored adsorbent 30 can be quickly distributed on each porous plate inside the fluidized floatingbed 30 by utilizing the potential energy of gravity. 11.

此外，预先贮存的吸附材可于该流体化浮动床10运转过程中，截取原本所超额供给的吸附材30而累积贮存；或者，预先贮存的吸附材可于该流体化浮动床10未运转之际，利用原有的吸附材供给机制而累积贮存，亦即可由该吸附材输送装置20延后关机而于该流体化浮动床10关机后预先累积贮存，或是于该流体化浮动床10开机前先令该吸附材输送装置20提早开机而预先累积贮存。因此，预先贮存于该快速供料贮槽60或该已脱附上输送槽28a的吸附材，该供料流量控制阀61可于该流体化浮动床10重新开机前让供料流量全开，使预先贮存的吸附材快速重新布满(用于重新开机)或快速补充(用于处理突发性高浓度待处理废气)于各该多孔板11上方；是以，本发明具有快速供给吸附材的功效。In addition, during the operation of the fluidized floatingbed 10, the pre-stored adsorbent material can intercept theexcess adsorbent material 30 and accumulate and store it; or, the pre-stored adsorbent material can be stored before the fluidized floatingbed 10 is not in operation. Actually, using the original adsorption material supply mechanism to accumulate and store, that is, the adsorptionmaterial conveying device 20 can delay shutdown and pre-accumulate and store after the fluidized floatingbed 10 is shut down, or start the fluidized floatingbed 10 Firstly, the adsorbent conveyingdevice 20 is started up early to accumulate and store in advance. Therefore, the feedflow control valve 61 can fully open the feed flow rate before restarting the fluidized floatingbed 10 for the adsorbent material stored in the fastfeed storage tank 60 or the desorbedupper delivery tank 28a in advance, Make the pre-stored adsorbent material quickly refill (for restarting the machine) or quickly replenish (for processing sudden high-concentration waste gas to be treated) above each of theporous plates 11; therefore, the present invention has the ability to quickly supply the adsorbent material effect.

以上所述，仅是本发明的较佳实施例而已，并非对本发明作任何形式上的限制，凡是依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与修饰，均仍属于本发明技术方案的范围内。The above are only preferred embodiments of the present invention, and are not intended to limit the present invention in any form. Any simple modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention still belong to within the scope of the technical solutions of the present invention.

综上所述，本发明在结构设计、使用实用性及成本效益上，完全符合产业发展所需，且所揭示的结构亦是具有前所未有的创新构造，具有新颖性、创造性、实用性，符合有关发明专利要件的规定，故依法提起申请。In summary, the present invention fully meets the needs of industrial development in terms of structural design, practicability and cost-effectiveness, and the disclosed structure also has an unprecedented innovative structure, novelty, creativity and practicability, and meets the requirements of relevant According to the requirements of the invention patent requirements, the application is filed according to law.

Claims (10)

1. fluidized floating bed adsorption material supply method, it is characterized in that, the adsorption material that will have adsorption capacity is stored in advance, and the position that makes adsorption material store in advance is higher than fluidized floating bed adsorption material inlet port, makes the adsorption material of storing in advance utilize gravitational potential energy and be distributed in fast fluidized floating bed.

2. fluidized floating bed adsorption material supply method according to claim 1 is characterized in that, described adsorption material of storing in advance in fluidized floating bed operation process, intercepting originally institute's excess supply adsorption material and accumulate storage.

3. fluidized floating bed adsorption material supply method according to claim 1 is characterized in that, described adsorption material of storing in advance utilizes original adsorption material supply mechanism and accumulation to store when fluidized floating bed not running.

4. the use cleaning system of described fluidized floating bed adsorption material supply method according to claim 1 is characterized in that, comprising:

One is fluidized floating bed, allows adsorption material successively drop down onto the bottom by the adsorption material inlet port importing on top and along several porous plates, and adsorb the organic compound in the pending waste gas;

One desorption column allows adsorption material be dropped down onto the bottom and the organic compound that adsorbs is added thermal desorption by the top;

One adsorption material conveying device is delivered to this desorption column top with the adsorption material that drops down onto this fluidized floating bed bottom, and the adsorption material that will drop down onto this desorption column bottom is delivered to the adsorption material inlet port on this fluidized floating bed top; And

One quick feed storage tank is arranged at this adsorption material conveying device in order to being linked to the absorption feed pipe of this adsorption material inlet port, and is provided with adsorption material feed streams control valve.

5. cleaning system according to claim 4, it is characterized in that, described adsorption material conveying device includes: carry source of the gas, treat delivery chute under the desorption, treat delivery chute on the desorption, delivery chute under the desorption, delivery chute on the desorption, link this fluidized floating bed bottom and the absorption discharge nozzle for the treatment of delivery chute under the desorption, link treat delivery chute under the desorption with treat delivery chute on the desorption treat the desorption carrier pipe, link the desorption feed pipe treat delivery chute and this desorption column top on the desorption, the desorption discharge nozzle that links delivery chute under this desorption column bottom and the desorption, the desorption carrier pipe that links delivery chute on delivery chute under the desorption and the desorption, the absorption feed pipe that links delivery chute and this adsorption material inlet port on the desorption, link this conveying source of the gas and treat treating the desorption gas source pipe and linking this conveyings source of the gas and the desorption gas source pipe of delivery chute under the desorption of delivery chute under the desorption.

6. according to claim 4 or 5 described cleaning systems, it is characterized in that, described flow control valve is in fluidized floating bed operation process, and control adsorption material feed flow is in order to intercepting the adsorption material of excess supply, and then accumulation is stored in this quick feed storage tank.

7. according to claim 4 or 5 described cleaning systems, it is characterized in that, described flow control valve cuts out fully in the fluidized floating bed not border of running, and borrows this adsorption material conveying device conveying adsorption material accumulation to be stored in this quick feed storage tank.

8. the use cleaning system of described method according to claim 1 is characterized in that, comprising:

One is fluidized floating bed, allows adsorption material successively drop down onto the bottom by the adsorption material inlet port importing on top and along several porous plates, and adsorb the organic compound in the pending waste gas;

One desorption column allows adsorption material be dropped down onto the bottom and the organic compound that adsorbs is added thermal desorption by the top;

One adsorption material conveying device, the adsorption material that drops down onto this fluidized floating bed bottom is delivered to this desorption column top, and the adsorption material that will drop down onto this desorption column bottom is delivered to the adsorption material inlet port on this fluidized floating bed top, and includes: carry source of the gas, treat delivery chute under the desorption, treat delivery chute on the desorption, delivery chute under the desorption, quick feed storage tank, link this fluidized floating bed bottom and the absorption discharge nozzle for the treatment of delivery chute under the desorption, link treat delivery chute under the desorption with treat delivery chute on the desorption treat the desorption carrier pipe, link the desorption feed pipe treat delivery chute and this desorption column top on the desorption, the desorption discharge nozzle that links delivery chute under this desorption column bottom and the desorption, link under the desorption delivery chute and the quick desorption carrier pipe of feed storage tank, the absorption feed pipe that links quick feed storage tank and this adsorption material inlet port, link this conveying source of the gas and treat treating the desorption gas source pipe and linking this conveyings source of the gas and the desorption gas source pipe of delivery chute under the desorption of delivery chute under the desorption; Yet, further make this desorption carrier pipe stretch into this on the desorption delivery chute inner, and be provided with adsorption material feed streams control valve in this absorption feed pipe.

9. cleaning system according to claim 8 is characterized in that, described flow control valve is in fluidized floating bed operation process, and control adsorption material feed flow is in order to intercepting the adsorption material of excess supply, and then accumulation is stored in this quick feed storage tank.

10. cleaning system according to claim 8 is characterized in that, described flow control valve cuts out fully in the fluidized floating bed not border of running, and borrows this adsorption material conveying device conveying adsorption material accumulation to be stored in this quick feed storage tank.

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