CN206597742U - A hydrocarbon cleaning device - Google Patents
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- CN206597742U CN206597742U CN201621262471.0U CN201621262471U CN206597742U CN 206597742 U CN206597742 U CN 206597742U CN 201621262471 U CN201621262471 U CN 201621262471U CN 206597742 U CN206597742 U CN 206597742U
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- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 95
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 95
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 95
- 238000004140 cleaning Methods 0.000 title claims abstract description 91
- 239000007788 liquid Substances 0.000 claims abstract description 101
- 238000004821 distillation Methods 0.000 claims abstract description 48
- 238000001035 drying Methods 0.000 claims abstract description 45
- 238000001816 cooling Methods 0.000 claims abstract description 24
- 238000009833 condensation Methods 0.000 claims abstract description 13
- 230000005494 condensation Effects 0.000 claims abstract description 13
- 239000007921 spray Substances 0.000 claims abstract 7
- 238000010438 heat treatment Methods 0.000 claims description 40
- 239000002699 waste material Substances 0.000 claims description 9
- 239000000498 cooling water Substances 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 11
- 229910052799 carbon Inorganic materials 0.000 claims 11
- 239000003795 chemical substances by application Substances 0.000 claims 11
- 239000003599 detergent Substances 0.000 claims 11
- 229910052739 hydrogen Inorganic materials 0.000 claims 11
- 239000001257 hydrogen Substances 0.000 claims 11
- 238000010926 purge Methods 0.000 claims 2
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 239000012459 cleaning agent Substances 0.000 abstract description 48
- 238000005406 washing Methods 0.000 abstract description 3
- 238000011084 recovery Methods 0.000 description 12
- 238000000034 method Methods 0.000 description 10
- 230000032258 transport Effects 0.000 description 5
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000007602 hot air drying Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000004506 ultrasonic cleaning Methods 0.000 description 1
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- Cleaning By Liquid Or Steam (AREA)
Abstract
Description
技术领域technical field
本实用新型涉及工业清洗领域,具体涉及一种碳氢清洗设备。The utility model relates to the field of industrial cleaning, in particular to a hydrocarbon cleaning device.
背景技术Background technique
在工业清洗行业中,许多工艺会应用到碳氢清洗技术,碳氢清洗设备和清洗流程也广为人知。如中国专利CN104056810A公开了一种具有防爆功能的碳氢清洗机,包括清洗槽,在所述清洗槽中有超声波震板,用抽气管道将超声波清洗槽中挥发的碳氢气体抽掉,清除了在清洗过程中产生的碳氢蒸汽,减少了爆炸危险。中国专利CN205351959U公开了一种碳氢清洗剂的干燥设备,包括干燥箱和用于朝干燥箱内鼓风的防爆风机,干燥箱和防爆机之间设有止回阀,提高了干燥过程安全性。中国专利CN202356344U公开了一种碳氢清洗设备的蒸汽浴洗系统,包括有清洗腔室与蒸汽发生器,采用高真空下对高温液体加热产生高温蒸汽的方式,蒸汽量大、蒸汽压力高,清洗效果更好,可降低能耗和减少安全隐患。中国专利CN202460162U公开了一种碳氢清洗设备的蒸馏回收系统,包括加热装置、蒸馏罐及冷凝回收器,该蒸馏回收系统采用真空泵使蒸馏罐保持高真空度,能够提高蒸馏效率。In the industrial cleaning industry, many processes will be applied to hydrocarbon cleaning technology, and hydrocarbon cleaning equipment and cleaning processes are also widely known. Disclosed a kind of hydrocarbon cleaning machine with explosion-proof function as Chinese patent CN104056810A, comprising a cleaning tank, in the cleaning tank, an ultrasonic shock plate is arranged, and the hydrocarbon gas volatilized in the ultrasonic cleaning tank is taken out with an air extraction pipeline, and the Eliminates the hydrocarbon vapors generated during the cleaning process, reducing the risk of explosion. Chinese patent CN205351959U discloses a drying equipment for hydrocarbon cleaning agents, including a drying box and an explosion-proof fan for blasting into the drying box. A check valve is provided between the drying box and the explosion-proof machine, which improves the safety of the drying process . Chinese patent CN202356344U discloses a steam bath washing system for hydrocarbon cleaning equipment, including a cleaning chamber and a steam generator, which adopts the method of heating high-temperature liquid under high vacuum to generate high-temperature steam, with large steam volume and high steam pressure, and easy cleaning The effect is better, which can reduce energy consumption and reduce safety hazards. Chinese patent CN202460162U discloses a distillation recovery system for hydrocarbon cleaning equipment, including a heating device, a distillation tank and a condensation recovery device. The distillation recovery system uses a vacuum pump to maintain a high vacuum in the distillation tank, which can improve distillation efficiency.
传统的工业清洗一般做法是将碳氢溶液盛装在清洗槽中,使工件、料带通过所述清洗槽的时候得到清洗,并且在清洗槽的后段设置一热风烘干槽,使工件或料带经过所述热风烘干槽时被热风冲刷烘干,防止将清洗液带出,也方便立即投入下一阶段的加工使用。但目前采用碳氢清洗技术中,产生的能耗较高,大部分的热量不易被回收利用。因此有必要提供一种新型的碳氢清洗设备,以提高碳氢清洗剂清洗过程的热量利用率。The general practice of traditional industrial cleaning is to fill the hydrocarbon solution in the cleaning tank, so that the workpiece and material belt can be cleaned when they pass through the cleaning tank, and a hot air drying tank is installed at the back of the cleaning tank to make the workpiece or material When the belt passes through the hot air drying tank, it is washed and dried by the hot air to prevent the cleaning liquid from being taken out, and it is also convenient to immediately put it into the next stage of processing and use. However, in the current hydrocarbon cleaning technology, the energy consumption is relatively high, and most of the heat is not easy to be recycled. Therefore, it is necessary to provide a novel hydrocarbon cleaning equipment to improve the heat utilization rate of the hydrocarbon cleaning agent cleaning process.
实用新型内容Utility model content
为解决上述问题,本实用新型提供了一种碳氢清洗设备,该碳氢清洗设备可以对碳氢清洗剂进行节能回收,提高了热量的利用效率。In order to solve the above problems, the utility model provides a hydrocarbon cleaning device, which can perform energy-saving recovery of the hydrocarbon cleaning agent and improve the utilization efficiency of heat.
本实用新型提供了一种碳氢清洗设备,包括清洗系统、第一冷却系统、蒸馏系统和干燥系统,所述清洗系统包括清洗槽,所述第一冷却系统包括第一冷凝器和环绕在所述第一冷凝器表面的第一冷凝盘管,所述蒸馏系统包括蒸馏罐,所述蒸馏罐设有出口和入口,所述干燥系统包括干燥槽、设在干燥槽顶部的喷淋器和设在干燥槽底部的收集口,所述第一冷凝器的一端与所述清洗槽连接用于将所述清洗槽中的碳氢清洗剂脏液持续输送至所述第一冷凝器中,所述第一冷凝器的另一端与所述入口连接用于将所述第一冷凝器中的碳氢清洗剂脏液输送至所述蒸馏罐中进行加热蒸馏,所述出口与所述喷淋器连接,使碳氢清洗剂脏液加热蒸馏产出的蒸汽通过所述喷淋器喷淋至所述干燥槽中用于干燥工件,所述收集口用于收集所述蒸汽在干燥过程中经冷凝形成的液体并输送至所述第一冷凝盘管中,所述第一冷凝器中的碳氢清洗剂脏液用于冷却所述第一冷凝盘管中的所述液体,得到碳氢清洗剂新液。The utility model provides a hydrocarbon cleaning device, comprising a cleaning system, a first cooling system, a distillation system and a drying system, the cleaning system includes a cleaning tank, the first cooling system includes a first condenser and The first condensing coil on the surface of the first condenser, the distillation system includes a distillation tank, the distillation tank is provided with an outlet and an inlet, and the drying system includes a drying tank, a sprayer arranged on the top of the drying tank and a device At the collection port at the bottom of the drying tank, one end of the first condenser is connected to the cleaning tank for continuously transporting the hydrocarbon cleaning agent dirty liquid in the cleaning tank to the first condenser, the The other end of the first condenser is connected to the inlet for transporting the hydrocarbon cleaning agent dirty liquid in the first condenser to the distillation tank for heating and distillation, and the outlet is connected to the sprayer , the steam produced by heating and distilling the dirty liquid of hydrocarbon cleaning agent is sprayed into the drying tank through the sprayer to dry the workpiece, and the collecting port is used to collect the steam to be formed by condensation during the drying process and transported to the first condensing coil, the hydrocarbon cleaning agent dirty liquid in the first condenser is used to cool the liquid in the first condensing coil to obtain a new hydrocarbon cleaning agent liquid.
优选地,所述碳氢清洗设备还包括第二冷却系统,所述第二冷却系统用于所述进一步冷却所述第一冷凝盘管输出的碳氢清洗剂新液。Preferably, the hydrocarbon cleaning equipment further includes a second cooling system, and the second cooling system is used for further cooling the new hydrocarbon cleaning agent liquid output from the first condensing coil.
优选地,所述第二冷却系统包括第二冷凝器和环绕在所述第二冷凝器表面的第二冷凝盘管,所述第一冷凝盘管输出的碳氢清洗剂新液进入所述第二冷凝器中,所述第二冷凝盘管中通有冷却水用于进一步冷却所述第二冷凝器中的碳氢清洗剂新液。Preferably, the second cooling system includes a second condenser and a second condensing coil surrounding the surface of the second condenser, and the new hydrocarbon cleaning agent liquid output from the first condensing coil enters the second condenser. In the second condenser, cooling water is passed through the second condensing coil for further cooling the new hydrocarbon cleaning agent liquid in the second condenser.
优选地,所述碳氢清洗设备还设有新液槽,所述新液槽用于储存所述碳氢清洗剂新液,所述新液槽与所述清洗槽通过自动阀门连接。Preferably, the hydrocarbon cleaning equipment is further provided with a new liquid tank for storing the new liquid of the hydrocarbon cleaning agent, and the new liquid tank is connected with the cleaning tank through an automatic valve.
优选地,所述清洗槽中设有液位控制系统,当所述清洗槽的液位低于目标液位时,所述新液槽内的所述碳氢清洗剂新液通过自动阀门进入到所述清洗槽中用于清洗工件。Preferably, a liquid level control system is provided in the cleaning tank, and when the liquid level in the cleaning tank is lower than the target liquid level, the new liquid of the hydrocarbon cleaning agent in the new liquid tank enters into the The cleaning tank is used for cleaning workpieces.
优选地,所述蒸馏系统还包括加热装置,所述加热装置用于加热蒸馏所述蒸馏罐中的碳氢清洗剂脏液。Preferably, the distillation system further includes a heating device for heating and distilling the hydrocarbon cleaning agent dirty liquid in the distillation tank.
优选地,所述加热装置包括加热盘管和导热油管,所述加热盘管设置在所述蒸馏罐的内部,所述导热油管设置在所述蒸馏罐的下方,所述加热盘管和导热油管中均通有导热油。Preferably, the heating device includes a heating coil and a heat-conducting oil pipe, the heating coil is arranged inside the distillation pot, the heat-conducting oil pipe is arranged below the distillation pot, the heating coil and the heat-conducting oil pipe There is heat transfer oil in the center.
优选地,所述加热盘管和所述导热油管均与导热油槽连接,所述导热油槽通过导热油泵分别将导热油输送至所述加热盘管和所述导热油管中。Preferably, both the heating coil and the heat-conducting oil pipe are connected to a heat-conducting oil tank, and the heat-conducting oil tank sends heat-conducting oil to the heating coil and the heat-conducting oil pipe respectively through a heat-conducting oil pump.
优选地,所述碳氢清洗设备还包括废液槽,所述蒸馏罐中产生的废液排至所述废液槽中。Preferably, the hydrocarbon cleaning equipment further includes a waste liquid tank, and the waste liquid generated in the distillation tank is discharged into the waste liquid tank.
本实用新型提供的节能可回收的碳氢清洗设备,既可以使得碳氢清洗剂能够有效回收,又充分利用了回收热量来保持清洗和回收温度;既节约了蒸馏罐中加热所需要的热量,又节约了冷却水的用量。The energy-saving and recyclable hydrocarbon cleaning equipment provided by the utility model can not only enable the effective recovery of the hydrocarbon cleaning agent, but also make full use of the recovered heat to maintain the cleaning and recovery temperature; it not only saves the heat required for heating in the distillation tank, It also saves the consumption of cooling water.
综上,本实用新型有益效果包括以下几个方面:In summary, the beneficial effects of the utility model include the following aspects:
1、本实用新型提供的节能可回收的碳氢清洗设备,既可以使得碳氢清洗剂能够有效回收,又充分利用了回收热量来保持清洗和回收温度;既节约了蒸馏罐中加热所需要的热量,又节约了冷却水的用量。1. The energy-saving and recyclable hydrocarbon cleaning equipment provided by the utility model can not only enable the effective recovery of hydrocarbon cleaning agents, but also make full use of the recovered heat to maintain the cleaning and recovery temperature; it saves the energy required for heating in the distillation tank heat, and save the amount of cooling water.
附图说明Description of drawings
图1为本实用新型一实施方式提供的一种碳氢清洗设备的结构示意图。Fig. 1 is a schematic structural diagram of a hydrocarbon cleaning device provided by an embodiment of the present invention.
具体实施方式detailed description
以下所述是本实用新型的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也视为本实用新型的保护范围。The following description is a preferred embodiment of the present utility model. It should be pointed out that for those of ordinary skill in the art, some improvements and modifications can also be made without departing from the principle of the present utility model. These improvements and modifications It is also regarded as the protection scope of the present utility model.
图1为本实用新型一实施方式提供的一种碳氢清洗设备的结构示意图,如图1所示,本实用新型提供了一种碳氢清洗设备,包括清洗系统1、第一冷却系统2、蒸馏系统3和干燥系统4,清洗系统1包括清洗槽11,第一冷却系统2包括第一冷凝器21和环绕在第一冷凝器表面的第一冷凝盘管22,蒸馏系统3包括蒸馏罐31,蒸馏罐设有入口311和出口312,干燥系统4包括干燥槽41、设在干燥槽顶部的喷淋器42和设在干燥槽底部的收集口43,第一冷凝器21的一端与清洗槽11连接用于将清洗槽11中的碳氢清洗剂脏液持续输送至第一冷凝器21中,第一冷凝器21的另一端与入口311连接用于将第一冷凝器21中的碳氢清洗剂脏液输送至蒸馏罐31中进行加热蒸馏,出口312与喷淋器42连接,使碳氢清洗剂脏液加热蒸馏产出的蒸汽通过喷淋器42喷淋至干燥槽41中用于干燥工件,收集口43用于收集蒸汽干燥过程中经冷凝形成的液体并输送至第一冷凝盘管22中,第一冷凝器中21的碳氢清洗剂脏液用于冷却第一冷凝盘管22中的液体,得到碳氢清洗剂新液。Fig. 1 is a schematic structural view of a hydrocarbon cleaning device provided by an embodiment of the present invention. As shown in Fig. 1, the utility model provides a hydrocarbon cleaning device, including a cleaning system 1, a first cooling system 2, Distillation system 3 and drying system 4, cleaning system 1 includes cleaning tank 11, first cooling system 2 includes first condenser 21 and first condensation coil 22 surrounding the surface of the first condenser, distillation system 3 includes distillation tank 31 , the distillation pot is provided with an inlet 311 and an outlet 312, and the drying system 4 includes a drying tank 41, a shower 42 arranged at the top of the drying tank and a collection port 43 located at the bottom of the drying tank, one end of the first condenser 21 is connected to the cleaning tank 11 is connected to continuously transport the hydrocarbon cleaning agent dirty liquid in the cleaning tank 11 to the first condenser 21, and the other end of the first condenser 21 is connected to the inlet 311 to transfer the hydrocarbon in the first condenser 21 The cleaning agent dirty liquid is transported to the distillation tank 31 for heating and distillation, and the outlet 312 is connected to the shower 42, so that the steam produced by the heating and distillation of the hydrocarbon cleaning agent dirty liquid is sprayed into the drying tank 41 through the shower 42 for To dry the workpiece, the collection port 43 is used to collect the liquid formed by condensation during the steam drying process and transport it to the first condensing coil 22, and the hydrocarbon cleaning agent dirty liquid in the first condenser 21 is used to cool the first condensing coil The liquid in 22, obtains the new liquid of hydrocarbon cleaning agent.
目前采用碳氢清洗技术尤其是蒸馏回收和热风烘干过程中,产生的能耗较高,大部分的热量不易被回收利用。At present, the use of hydrocarbon cleaning technology, especially in the process of distillation recovery and hot air drying, produces high energy consumption, and most of the heat is not easy to be recycled.
本实用新型提供的碳氢清洗设备,第一冷凝盘管中的液体被冷凝器中的碳氢清洗剂脏液冷却从而降温,同时冷凝器中的碳氢清洗剂脏液温度也得到了提高,一方面,使用碳氢清洗剂脏液作为冷却介质,节约了冷却水的用量。另一方面,充分利用了蒸汽在干燥过程中经冷凝形成的液体的热量,对碳氢清洗剂脏液进行预热,使碳氢清洗剂脏液温度提高,节约了后续蒸馏罐中加热所需要的热量。因此本实用新型提供的碳氢清洗设备提高碳氢清洗剂蒸馏回收和干燥过程中的热量的利用率。In the hydrocarbon cleaning equipment provided by the utility model, the liquid in the first condensing coil is cooled by the dirty liquid of the hydrocarbon cleaning agent in the condenser to lower the temperature, and at the same time, the temperature of the dirty liquid of the hydrocarbon cleaning agent in the condenser is also increased. On the one hand, the use of hydrocarbon cleaning agent dirty liquid as the cooling medium saves the amount of cooling water. On the other hand, the heat of the liquid formed by condensation of the steam during the drying process is fully utilized to preheat the dirty liquid of the hydrocarbon cleaning agent, so that the temperature of the dirty liquid of the hydrocarbon cleaning agent is increased, saving the heating required in the subsequent distillation tank of heat. Therefore, the hydrocarbon cleaning equipment provided by the utility model improves the utilization rate of the heat in the distillation recovery and drying process of the hydrocarbon cleaning agent.
本实用新型中,蒸馏罐的入口311设置在蒸馏罐的底部。In the present invention, the inlet 311 of the distillation tank is arranged at the bottom of the distillation tank.
本实用新型中,蒸馏罐的出口312设置在蒸馏罐的顶部。In the utility model, the outlet 312 of the distillation tank is arranged on the top of the distillation tank.
本实用新型中,清洗槽底部设有碳氢清洗剂脏液出口,碳氢清洗剂脏液出口与第一冷凝器21连接。In the utility model, the bottom of the cleaning tank is provided with a hydrocarbon cleaning agent dirty liquid outlet, and the hydrocarbon cleaning agent dirty liquid outlet is connected to the first condenser 21 .
本实用新型中,清洗系统可以包括至少一个清洗槽。每个清洗槽中的碳氢清洗剂脏液均可持续输送至第一冷凝器21中。In the present utility model, the cleaning system may include at least one cleaning tank. The hydrocarbon cleaning agent dirty liquid in each cleaning tank can be continuously sent to the first condenser 21 .
本实用新型中,碳氢清洗设备还包括第二冷却系统,第二冷却系统用于进一步冷却第一冷凝盘管输出的碳氢清洗剂新液。In the utility model, the hydrocarbon cleaning equipment further includes a second cooling system, and the second cooling system is used for further cooling the new hydrocarbon cleaning agent liquid output by the first condensation coil.
本实用新型中,第二冷却系统包括第二冷凝器和环绕在第二冷凝器表面的第二冷凝盘管,第一冷凝盘管输出的碳氢清洗剂新液进入第二冷凝器中,第二冷凝盘管中通有冷却水用于进一步冷却第二冷凝器中的碳氢清洗剂新液。In the utility model, the second cooling system includes a second condenser and a second condensing coil surrounding the surface of the second condenser. The new hydrocarbon cleaning agent output from the first condensing coil enters the second condenser. Cooling water is passed through the second condensing coil to further cool the new liquid of the hydrocarbon cleaning agent in the second condenser.
为进一步冷却碳氢清洗剂新液,本实用新型还提供了第二冷却系统,第二冷凝盘管中可以通入冷却水或者通入其他冷却介质。In order to further cool the new liquid of the hydrocarbon cleaning agent, the utility model also provides a second cooling system, and cooling water or other cooling media can be fed into the second condensing coil.
本实用新型中,碳氢清洗设备还设有新液槽5,新液槽5用于储存碳氢清洗剂新液,新液槽5与清洗槽11通过自动阀门连接。In the utility model, the hydrocarbon cleaning equipment is also provided with a new liquid tank 5, the new liquid tank 5 is used to store the new liquid of the hydrocarbon cleaning agent, and the new liquid tank 5 is connected with the cleaning tank 11 through an automatic valve.
本实用新型中,清洗槽中设有液位控制系统,当清洗槽的液位低于目标液位时,新液槽内的碳氢清洗剂新液通过自动阀门进入到清洗槽中用于清洗工件。In the utility model, a liquid level control system is provided in the cleaning tank. When the liquid level of the cleaning tank is lower than the target liquid level, the new liquid of the hydrocarbon cleaning agent in the new liquid tank enters the cleaning tank through an automatic valve for cleaning. artifact.
本实用新型中,蒸馏系统还包括加热装置,加热装置用于加热蒸馏蒸馏罐中的碳氢清洗剂脏液。In the utility model, the distillation system further includes a heating device, which is used for heating the dirty liquid of the hydrocarbon cleaning agent in the distillation tank.
本实用新型中,加热装置包括加热盘管和导热油管,加热盘管设置在蒸馏罐的内部,导热油管设置在蒸馏罐的下方,加热盘管和导热油管中均通有导热油。In the utility model, the heating device includes a heating coil and a heat-conducting oil pipe. The heating coil is arranged inside the retort, and the heat-conducting oil pipe is arranged below the retort. Both the heating coil and the heat-conducting oil pipe are connected with heat-conducting oil.
本实用新型中,加热盘管和导热油管均与导热油槽连接,导热油槽通过导热油泵将导热油分别输送至加热盘管和导热油管中。In the utility model, both the heating coil and the heat-conducting oil pipe are connected with the heat-conducting oil tank, and the heat-conducting oil tank transports the heat-conducting oil to the heating coil and the heat-conducting oil pipe respectively through the heat-conducting oil pump.
加热装置对蒸馏罐的底部以及内部进行加热,导热油泵将导热油槽内的导热油输送至导热油管和加热盘管中对碳氢清洗剂脏液进行加热。两种加热方式相结合,加热更加直接,接触面积更大。The heating device heats the bottom and inside of the distillation tank, and the heat-conducting oil pump transports the heat-conducting oil in the heat-conducting oil tank to the heat-conducting oil pipe and the heating coil to heat the dirty liquid of the hydrocarbon cleaning agent. Combining the two heating methods, the heating is more direct and the contact area is larger.
本实用新型中,碳氢清洗设备还包括废液槽,蒸馏罐中产生的废液排至废液槽中。In the utility model, the hydrocarbon cleaning equipment also includes a waste liquid tank, and the waste liquid generated in the distillation tank is discharged into the waste liquid tank.
本实用新型碳氢清洗剂脏液加热蒸馏产出的蒸汽通过喷淋器喷淋至干燥槽中,用于对工件进行蒸汽清洗,深度清洗后工件表面残留的蒸汽小液滴经过自然干燥,与没有进行蒸汽清洗的工件相比,本实用新型干燥时间得到大量缩短。这样,既对工件进行了深度清洗,又缩短了干燥时间,同时充分利用了蒸馏产生的高温蒸汽的热量。The steam produced by heating and distilling the dirty liquid of the hydrocarbon cleaning agent of the utility model is sprayed into the drying tank through the sprayer, and is used to steam clean the workpiece. Compared with workpieces not cleaned by steam, the drying time of the utility model is greatly shortened. In this way, the workpiece is deeply cleaned, and the drying time is shortened, and at the same time, the heat of the high-temperature steam generated by distillation is fully utilized.
本实用新型中,蒸汽的温度为160℃-190℃。In the utility model, the temperature of the steam is 160°C-190°C.
本实用新型中,干燥后,所述蒸汽在干燥过程中经冷凝形成的液体的温度为140℃-150℃。In the present invention, after drying, the temperature of the liquid formed by condensation of the steam during the drying process is 140°C-150°C.
本实用新型中,所述第一冷凝器中的碳氢清洗剂脏液用于冷却所述第一冷凝盘管中的所述液体,换热后,第一冷凝器中的碳氢清洗剂脏液的温度可以达到85℃-125℃。从清洗槽出来的碳氢清洗剂脏液的温度为40℃-45℃,与较热的液体换热后,温度可上升至85℃-125℃。In the utility model, the hydrocarbon cleaning agent dirty liquid in the first condenser is used to cool the liquid in the first condensation coil, after heat exchange, the hydrocarbon cleaning agent in the first condenser is dirty The temperature of the liquid can reach 85°C-125°C. The temperature of the hydrocarbon cleaning agent dirty liquid coming out of the cleaning tank is 40°C-45°C, and after exchanging heat with the hotter liquid, the temperature can rise to 85°C-125°C.
本实用新型中,相比于现有的碳氢清洗设备,本实用新型提供的碳氢清洗设备的热量利用率可达到40%以上。In the utility model, compared with the existing hydrocarbon cleaning equipment, the heat utilization rate of the hydrocarbon cleaning equipment provided by the utility model can reach more than 40%.
本实用新型中,喷淋器通过常规的方式设置在干燥槽的顶部。In the utility model, the sprayer is arranged on the top of the drying tank in a conventional manner.
本实用新型中,喷淋器的数量为至少一个。In the present utility model, the number of the sprayer is at least one.
本实用新型中,干燥槽的数量为至少一个。可以在一个干燥槽顶部设置多个喷淋器,也可以设置多个干燥槽从而在每个干燥槽顶部均设置至少一个喷淋器。In the utility model, the number of drying tanks is at least one. A plurality of showers can be arranged on the top of one drying tank, or a plurality of drying tanks can be arranged so that at least one shower is arranged on the top of each drying tank.
本实用新型中,当干燥槽的数量为多个时,每个干燥槽底部的收集口收集得到的液体混合后一起输送至第一冷凝盘管中。In the present invention, when there are multiple drying tanks, the liquid collected by the collecting port at the bottom of each drying tank is mixed and transported to the first condensation coil together.
本实用新型提供的碳氢清洗设备的应用过程具体为:将清洗槽中的碳氢清洗剂脏液持续输送至第一冷凝器中,然后从第一冷凝器中进入蒸馏罐进行加热蒸馏,加热蒸馏产生的蒸汽通过出口进入喷淋器,通过喷淋器喷淋至干燥槽中用于干燥工件,干燥后,收集蒸汽干燥过程中冷凝形成的液体进入第一冷凝盘管中,此时,冷凝器中的碳氢清洗剂脏液用于冷却第一冷凝盘管中的液体,得到碳氢清洗剂新液。同时,第一冷凝器中的碳氢清洗剂脏液也得到了预热,温度升高,后续再进入蒸馏罐进行蒸馏。整个过程循环进行。当清洗槽的液位低于目标液位时,新液罐内的新液进入到清洗槽用于清洗工件。The application process of the hydrocarbon cleaning equipment provided by the utility model is specifically: continuously transport the dirty liquid of the hydrocarbon cleaning agent in the cleaning tank to the first condenser, and then enter the distillation tank from the first condenser for heating and distillation, heating The steam generated by distillation enters the sprayer through the outlet, and is sprayed into the drying tank through the sprayer to dry the workpiece. After drying, the liquid formed by condensation during the steam drying process is collected and entered into the first condensation coil. At this time, the condensed The hydrocarbon cleaning agent dirty liquid in the tank is used to cool the liquid in the first condensing coil to obtain a new hydrocarbon cleaning agent liquid. At the same time, the hydrocarbon cleaning agent dirty liquid in the first condenser is also preheated, the temperature rises, and then enters the distillation tank for distillation. The whole process is cyclical. When the liquid level of the cleaning tank is lower than the target liquid level, the new liquid in the new liquid tank enters the cleaning tank for cleaning the workpiece.
本实用新型提供的节能可回收的碳氢清洗设备,既可以使得碳氢清洗剂能够有效回收,又充分利用了回收热量来保持清洗和回收温度;既节约了蒸馏罐中加热所需要的热量,又节约了冷却水的用量。The energy-saving and recyclable hydrocarbon cleaning equipment provided by the utility model can not only enable the effective recovery of the hydrocarbon cleaning agent, but also make full use of the recovered heat to maintain the cleaning and recovery temperature; it not only saves the heat required for heating in the distillation tank, It also saves the consumption of cooling water.
以上所述实施例仅表达了本实用新型的几种实施方式,其描述较为具体和详细,但并不能因此而理解为对本实用新型专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本实用新型构思的前提下,还可以做出若干变形和改进,这些都属于本实用新型的保护范围。因此,本实用新型专利的保护范围应以所附权利要求为准。The above-mentioned embodiments only express several implementations of the utility model, and the description thereof is relatively specific and detailed, but it should not be construed as limiting the patent scope of the utility model. It should be noted that those skilled in the art can make several modifications and improvements without departing from the concept of the present invention, and these all belong to the protection scope of the present invention. Therefore, the scope of protection of the utility model patent should be based on the appended claims.
Claims (9)
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