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CN101864329B - Wet purification method of sequencing batch biomass gas - Google Patents

Wet purification method of sequencing batch biomass gas Download PDF

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CN101864329B
CN101864329B CN201010211248.4A CN201010211248A CN101864329B CN 101864329 B CN101864329 B CN 101864329B CN 201010211248 A CN201010211248 A CN 201010211248A CN 101864329 B CN101864329 B CN 101864329B
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CN101864329A (en
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龚惠娟
陈泽智
王巧玲
肖文平
姜茹
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Nanjing University
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Abstract

一种批序式生物质气体湿式净化方法,其特征是它由吸收和再生二个阶段交替进行,且在同一个塔内完成,无需外加处理设备,因此具有占地面积小,投资少的优点。

A batch-type biomass gas wet purification method, which is characterized in that it is carried out alternately by two stages of absorption and regeneration, and is completed in the same tower without additional processing equipment, so it has the advantages of small footprint and low investment .

Description

批序式生物质气体湿式净化方法Batch type biomass gas wet purification method

技术领域 technical field

本发明涉及一种生物质气体净化处理方法,尤其是一种适合于中小型生产规模的生物质气体处理领域的湿式净化方法,具体地说是一种批序式生物质气体湿式净化方法。The invention relates to a biomass gas purification treatment method, in particular to a wet purification method suitable for small and medium-sized production scale biomass gas treatment fields, in particular to a batch-type biomass gas wet purification method.

背景技术 Background technique

众所周知,生物质气体在利用过程中,根据场合要求需要进行气体净化处理,其中要去除的组分主要有硫化氢、二氧化碳等。脱硫的目的在于防止设备腐蚀,而脱除二氧化碳主要用于提高燃气热值,减少气体中的阻燃性气体含量。湿式脱硫和湿式脱碳已经成为生物质气体净化的主要技术,比如DDS、PDS、络合铁法、萘醌法等湿式脱硫技术以及包含MDEA、DHA等工艺在内的湿式脱碳技术,这些技术的最大特点是可以对原料气体进行连续式净化处理,即原料气在吸收塔内被吸收液进行吸收净化,从吸收塔排出的吸收液(富液)在塔外采用加热或空气氧化(曝气)等方式进行再生,再生后的吸收液(贫液)重新进入吸收塔工作。这种方法在生物质气体净化领域中进行应用出现了一些需要解决或改进的问题,诸如存在系统流程复杂、占地面积大、投资高的问题,限制了在中小型生物质气体利用领域内的应用。As we all know, during the utilization of biomass gas, gas purification treatment is required according to the requirements of the occasion, and the components to be removed mainly include hydrogen sulfide and carbon dioxide. The purpose of desulfurization is to prevent corrosion of equipment, while the removal of carbon dioxide is mainly used to increase the calorific value of gas and reduce the content of flame retardant gases in the gas. Wet desulfurization and wet decarbonization have become the main technologies for biomass gas purification, such as wet desulfurization technologies such as DDS, PDS, complex iron method, naphthoquinone method, and wet decarbonization technologies including MDEA, DHA and other processes. These technologies The biggest feature is that the raw material gas can be continuously purified, that is, the raw material gas is absorbed and purified by the absorption liquid in the absorption tower, and the absorption liquid (rich liquid) discharged from the absorption tower is heated or air oxidized (aeration) outside the tower. ) and other ways to regenerate, and the regenerated absorption liquid (poor liquid) re-enters the absorption tower to work. The application of this method in the field of biomass gas purification has some problems that need to be solved or improved, such as the problems of complex system flow, large floor area, and high investment, which limit the application in the field of small and medium-sized biomass gas utilization. application.

发明内容 Contents of the invention

本发明的目的是针对现有的湿式生物质气体净化处理过程中存在的流程复杂、设备占地面积大,投资高、不适合于中小型生产规模的生物质气体回收利用的问题,发明一种占地面积小,工艺流程简单,适应范围广的批序式生物质气体湿式净化方法。The purpose of the present invention is to solve the problems in the existing wet biomass gas purification process, such as complex process, large equipment footprint, high investment, and unsuitable for the recovery and utilization of biomass gas in small and medium-sized production scales, and to invent a Small footprint, simple process flow, and a wide range of batch-type biomass gas wet purification methods.

本发明的技术方案是:Technical scheme of the present invention is:

一种批序式生物质气体湿式净化方法,其特征是它包括以下步骤:A batch type biomass gas wet purification method is characterized in that it comprises the following steps:

首先,在吸收塔的底部设置一个储液槽;First, set a liquid storage tank at the bottom of the absorption tower;

其次,将吸收液再生装置安装在所述的储液槽内;Secondly, the absorption liquid regeneration device is installed in the liquid storage tank;

第三,在吸收塔的上部设置一个再生排放气管;Third, set a regeneration exhaust gas pipe on the upper part of the absorption tower;

第四,打开原料气进气管,关闭再生排放气管,利用循环泵将储液槽内的吸收液泵入吸收塔的上部向下喷淋,使上行的原料气与下落的吸收液进行逆向接触,实现对原料气的净化,净化后的原料气从净化气管排出吸收塔,吸收液下落到储液槽内被循环泵不断地泵入吸收塔上部的喷淋头中向下喷淋,如此循环;Fourth, open the raw material gas inlet pipe, close the regeneration exhaust gas pipe, use the circulation pump to pump the absorption liquid in the liquid storage tank into the upper part of the absorption tower and spray downwards, so that the upward raw material gas and the falling absorption liquid are in reverse contact, To realize the purification of the raw material gas, the purified raw gas is discharged from the absorption tower from the purified gas pipe, and the absorption liquid falls into the liquid storage tank and is continuously pumped into the spray head on the upper part of the absorption tower by the circulation pump to spray downwards, thus circulating;

第五,重复第四步约25-35分钟后,关闭原料气进气管,打开再生排放气管,启动吸收液再生装置使之连续工作15-25分钟,完成吸收液的再生工作后即后重复第四步再次对新的原料气进行净化再生,如此循环,实现批序式生物质气体的湿式净化过程。Fifth, after repeating the fourth step for about 25-35 minutes, close the raw gas inlet pipe, open the regeneration exhaust pipe, start the absorption liquid regeneration device to work continuously for 15-25 minutes, and repeat the first step after completing the regeneration of the absorption liquid The new raw material gas is purified and regenerated again in four steps, and this cycle realizes the wet purification process of batch-type biomass gas.

其中的吸收液再生装置可为换热器式吸收液再生装置,再生时,先向换热器中通入蒸汽对吸收液进行加热再生10-15分钟,再生过程中产生的再生气从吸收塔上部的再生排放气管排出,再生结束后再向换热器中通入冷却水使之循环5-10分钟对吸收液进行冷却即可。The absorption liquid regeneration device can be a heat exchanger-type absorption liquid regeneration device. When regenerating, first pass steam into the heat exchanger to heat and regenerate the absorption liquid for 10-15 minutes. The regeneration gas generated during the regeneration process is discharged from the absorption tower The upper part of the regeneration exhaust pipe is discharged, and after the regeneration is completed, the cooling water is passed into the heat exchanger to circulate for 5-10 minutes to cool the absorption liquid.

所述的吸收液再生装置还可为曝气管式吸收液再生装置,再生时利用曝气管向储液槽内的吸收液曝气15-25分钟即可,再生过程中产生的再生气从吸收塔上部的再生排放气管排出。The absorption liquid regeneration device can also be an aeration tube type absorption liquid regeneration device. During regeneration, the aeration tube can be used to aerate the absorption liquid in the liquid storage tank for 15-25 minutes, and the regeneration gas generated in the regeneration process is from The regeneration discharge gas pipe at the upper part of the absorption tower is discharged.

本发明的有益效果:Beneficial effects of the present invention:

本发明既发挥了湿式净化法所具有有高净化效率的特性,又避免了传统的湿式净化法所具有来的系统流程复杂、占地面积大、投资高的问题,本发明的最大特点是将以往为外置式的蒸汽加热或空气鼓吹氧化再生段,移入到吸收塔底部的储液槽内,使得吸收液洗涤净化与吸收液再生是在一个塔体内完成,这样还可以省略对液位控制、流量平衡、压力平衡等方面的要求,从而大大简化了工艺流程,使得设备占地面积小、投资减少。The present invention not only brings into play the characteristics of high purification efficiency of the wet purification method, but also avoids the problems of complex system flow, large floor area and high investment of the traditional wet purification method. The biggest feature of the present invention is that the In the past, the external steam heating or air blowing oxidation regeneration section was moved into the liquid storage tank at the bottom of the absorption tower, so that the washing and purification of the absorption liquid and the regeneration of the absorption liquid were completed in one tower, so that the control of liquid level, Flow balance, pressure balance and other requirements, thus greatly simplifying the process flow, making the equipment occupy a small area and reduce investment.

本发明的吸收和再生在同一个塔内交替进行,吸收一定时间后再进行再生,再生结束后再进行吸收。Absorption and regeneration in the present invention are carried out alternately in the same tower, and regeneration is carried out after a certain period of time after absorption, and absorption is carried out after completion of regeneration.

附图说明Description of drawings

图1是本发明的批序式生物质气体湿式净化工艺流程图。Fig. 1 is a flow chart of the batch-sequential biomass gas wet purification process of the present invention.

具体实施方式 Detailed ways

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

如图1所示。As shown in Figure 1.

一种批序式生物质气体湿式净化方法,它包括以下步骤:A batch type biomass gas wet purification method, it comprises the following steps:

首先,在吸收塔1的底部设置一个储液槽2,必要时还应为储液槽增加一个吸收液补液装置3,以弥补净化过程中减少的吸收液,使储液槽的液位始终保持在一个水平;First of all, a liquid storage tank 2 is set at the bottom of the absorption tower 1. If necessary, an absorption liquid replenishment device 3 should be added to the liquid storage tank to make up for the reduced absorption liquid during the purification process, so that the liquid level of the liquid storage tank is always maintained. at a level;

其次,将吸收液再生装置4安装在所述的储液槽2内;Secondly, the absorption liquid regeneration device 4 is installed in the liquid storage tank 2;

第三,在吸收塔的上部设置一个再生排放气管;Third, set a regeneration exhaust gas pipe on the upper part of the absorption tower;

第四,打开原料气进气管5,关闭再生排放气管6,利用循环泵7将储液槽2内的吸收液泵入吸收塔1的上部向下喷淋,使上行的原料气与下落的吸收液进行逆向接触,实现对原料气的净化,净化后的原料气从净化气管8排出吸收塔1,吸收液下落到储液槽2内被循环泵7不断地泵入吸收塔1上部的喷淋头中向下喷淋,如此循环;Fourth, open the raw material gas inlet pipe 5, close the regeneration exhaust gas pipe 6, use the circulation pump 7 to pump the absorption liquid in the liquid storage tank 2 into the upper part of the absorption tower 1 and spray downwards, so that the upward raw material gas and the falling absorption The liquid is reversely contacted to realize the purification of the raw material gas. The purified raw gas is discharged from the absorption tower 1 from the purified gas pipe 8, and the absorption liquid falls into the liquid storage tank 2 and is continuously pumped into the upper part of the absorption tower 1 by the circulation pump 7. Spray downwards in the head, and so on;

第五,重复第四步约25-35分钟后,关闭原料气进管5,打开再生排放气管6,启动吸收液再生装置4使之连续工作15-25分钟,完成吸收液的再生工作后即后重复第四步再次对新的原料气进行净化再生,如此循环,实现批序式生物质气体的湿式净化过程。Fifth, after repeating the fourth step for about 25-35 minutes, close the raw material gas inlet pipe 5, open the regeneration discharge gas pipe 6, start the absorption liquid regeneration device 4 to make it work continuously for 15-25 minutes, and complete the regeneration of the absorption liquid. Then repeat the fourth step to purify and regenerate the new raw material gas again. This cycle realizes the wet purification process of batch-type biomass gas.

具体实施时,吸收液再生装置4可采用现有的换热器式吸收液再生装置,再生时,先向换热器中通入蒸汽对吸收液进行加热再生10-15分钟,再生过程中产生的再生气从吸收塔上部的再生排放气管排出,再生结束后再向换热器中通入冷却水使之循环5-10分钟对吸收液进行冷却即可。During specific implementation, the absorption liquid regeneration device 4 can adopt the existing heat exchanger type absorption liquid regeneration device. During regeneration, first feed steam into the heat exchanger to heat and regenerate the absorption liquid for 10-15 minutes. The regenerated gas is discharged from the regeneration exhaust pipe on the upper part of the absorption tower, and after the regeneration is completed, the cooling water is passed into the heat exchanger to circulate for 5-10 minutes to cool the absorption liquid.

所述的吸收液再生装置还可采用现有的曝气管式吸收液再生装置,再生时利用曝气管向储液槽内的吸收液曝气15-25分钟即可,再生过程中产生的再生气从吸收塔上部的再生排放气管排出。The absorption liquid regeneration device can also adopt the existing aeration tube type absorption liquid regeneration device. When regenerating, use the aeration tube to aerate the absorption liquid in the liquid storage tank for 15-25 minutes. The regeneration gas is discharged from the regeneration exhaust pipe at the upper part of the absorption tower.

从上可见,本发明的吸收液对气体的吸收净化以及吸收液的再生这两个工作段,是在一个塔体内完成,因此具有体积小,适应范围广的特点,它既适用于大型生物质气体应用领域,尤其适用于中小型生产规模的生物质气体应用领域。本发明可应用于脱除生物质气体中的硫化氢、二氧化碳等气体净化装置中。It can be seen from the above that the absorption and purification of gas by the absorption liquid and the regeneration of the absorption liquid in the present invention are completed in one tower body, so it has the characteristics of small volume and wide adaptability, and it is suitable for large biomass Gas application field, especially suitable for small and medium-sized production scale biomass gas application field. The invention can be applied to gas purification devices for removing hydrogen sulfide, carbon dioxide and the like in biomass gas.

本发明的运行特点为:当进行气体吸收分离净化时,原料气管打开,再生排放气管关闭,原料气从吸收塔下部进入,由下向上在吸收段9内(可以是填料区、空心喷洒区、鼓泡塔板等)与吸收液进行逆向接触,净化后的气体由净化气管排出,吸收液由循环泵进行循环吸收;当吸收液循环吸收原料气到一定阶段后,吸收液的吸收容量接近饱和,切换到再生工作状态,此时关闭原料气管,打开再生排放气管,开启再生装置(可以是换热器或曝气管等),在再生过程中产生的再生气由再生气管排出。The operating characteristics of the present invention are: when performing gas absorption, separation and purification, the raw material gas pipe is opened, the regeneration discharge gas pipe is closed, the raw material gas enters from the bottom of the absorption tower, and enters from the bottom up in the absorption section 9 (which can be a packing area, a hollow spraying area, bubbling trays, etc.) are in reverse contact with the absorption liquid, the purified gas is discharged from the purification gas pipe, and the absorption liquid is circulated and absorbed by the circulating pump; when the absorption liquid absorbs the raw material gas to a certain stage, the absorption capacity of the absorption liquid is close to saturation , switch to the regeneration working state, at this time close the raw material gas pipe, open the regeneration discharge gas pipe, open the regeneration device (it can be a heat exchanger or aeration pipe, etc.), and the regeneration gas generated during the regeneration process is discharged from the regeneration gas pipe.

本发明未涉及部分均与现有技术相同或可采用现有技术加以实现。The parts not involved in the present invention are the same as the prior art or can be realized by adopting the prior art.

Claims (1)

1.一种批序式生物质气体湿式净化方法,其特征是它包括以下步骤:1. A batch type biomass gas wet purification method is characterized in that it comprises the following steps: 首先,在吸收塔的底部设置一个储液槽;First, set a liquid storage tank at the bottom of the absorption tower; 其次,将吸收液再生装置安装在所述的储液槽内;Secondly, the absorption liquid regeneration device is installed in the liquid storage tank; 第三,在吸收塔的上部设置一个再生排放气管;Third, set a regeneration exhaust gas pipe on the upper part of the absorption tower; 第四,打开原料气进气管,关闭再生排放气管,利用循环泵将储液槽内的吸收液泵入吸收塔的上部向下喷淋,使上行的原料气与下落的吸收液进行逆向接触,实现对原料气的净化,净化后的原料气从净化气管排出吸收塔,吸收液下落到储液槽内被循环泵不断地泵入吸收塔上部的喷淋头中向下喷淋,如此循环;Fourth, open the raw material gas inlet pipe, close the regeneration exhaust gas pipe, use the circulation pump to pump the absorption liquid in the liquid storage tank into the upper part of the absorption tower and spray downwards, so that the upward raw material gas and the falling absorption liquid are in reverse contact, To realize the purification of the raw material gas, the purified raw gas is discharged from the absorption tower from the purified gas pipe, and the absorption liquid falls into the liquid storage tank and is continuously pumped into the spray head on the upper part of the absorption tower by the circulation pump to spray downwards, thus circulating; 第五,重复第四步约25-35分钟后,关闭原料气进气管,打开再生排放气管,启动吸收液再生装置使之连续工作15-25分钟,完成吸收液的再生工作后即后重复第四步再次对新的原料气进行净化再生,如此循环,实现批序式生物质气体的湿式净化过程;Fifth, after repeating the fourth step for about 25-35 minutes, close the raw gas inlet pipe, open the regeneration exhaust pipe, start the absorption liquid regeneration device to work continuously for 15-25 minutes, and repeat the first step after completing the regeneration of the absorption liquid Purify and regenerate the new raw material gas again in four steps, so that the cycle can realize the wet purification process of batch-type biomass gas; 所述的吸收液再生装置为曝气管式吸收液再生装置或换热器式吸收液再生装置,曝气管式吸收液再生装置再生时利用曝气管向储液槽内的吸收液曝气15-25分钟即可,再生过程中产生的再生气从吸收塔上部的再生排放气管排出;换热器式吸收液再生装置再生时,先向换热器中通入蒸汽对吸收液进行加热再生10-15分钟,再生过程中产生的再生气从吸收塔上部的再生排放气管排出,再生结束后再向换热器中通入冷却水使之循环5-10分钟对吸收液进行冷却即可。The absorption liquid regeneration device is an aeration tube type absorption liquid regeneration device or a heat exchanger type absorption liquid regeneration device, and the aeration tube is used to aerate the absorption liquid in the liquid storage tank when the aeration tube type absorption liquid regeneration device is regenerated It takes 15-25 minutes, and the regeneration gas generated during the regeneration process is discharged from the regeneration exhaust pipe on the upper part of the absorption tower; when the heat exchanger type absorption liquid regeneration device is regenerated, steam is first passed into the heat exchanger to heat and regenerate the absorption liquid After 10-15 minutes, the regeneration gas generated during the regeneration process is discharged from the regeneration exhaust pipe on the upper part of the absorption tower. After the regeneration is completed, the cooling water is passed into the heat exchanger to circulate for 5-10 minutes to cool the absorption liquid.
CN201010211248.4A 2010-06-25 2010-06-25 Wet purification method of sequencing batch biomass gas Expired - Fee Related CN101864329B (en)

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CN101327395A (en) * 2008-05-16 2008-12-24 贡有成 Sequencing batch limestone slurry wet desulfurization technique

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