WO2015101053A1 - Spraying separator device - Google Patents
Spraying separator device Download PDFInfo
- Publication number
- WO2015101053A1 WO2015101053A1 PCT/CN2014/084997 CN2014084997W WO2015101053A1 WO 2015101053 A1 WO2015101053 A1 WO 2015101053A1 CN 2014084997 W CN2014084997 W CN 2014084997W WO 2015101053 A1 WO2015101053 A1 WO 2015101053A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- chilled water
- housing
- heat exchange
- gas cooler
- waste gas
- Prior art date
Links
- 238000005507 spraying Methods 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 239000010865 sewage Substances 0.000 claims description 28
- 239000007921 spray Substances 0.000 claims description 13
- 239000002912 waste gas Substances 0.000 claims 7
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 18
- 229920000297 Rayon Polymers 0.000 description 11
- 239000000835 fiber Substances 0.000 description 10
- 239000007789 gas Substances 0.000 description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 229920002678 cellulose Polymers 0.000 description 5
- 239000001913 cellulose Substances 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 238000013461 design Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 description 3
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000012991 xanthate Substances 0.000 description 3
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 206010041235 Snoring Diseases 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000007380 fibre production Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 230000004630 mental health Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 238000002166 wet spinning Methods 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 1
- 229960001763 zinc sulfate Drugs 0.000 description 1
- 229910000368 zinc sulfate Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
Definitions
- the invention relates to one.
- it relates to a spray separator device which is one of the core equipment for carbon disulfide recovery in the fiber manufacturing process.
- Viscose fiber is one of the first chemical fibers to be industrially produced. Because of its good hygroscopicity, comfortable wearing and excellent spinnability, it is often blended with cotton, wool or various synthetic fibers, interwoven, used in all kinds of clothing and decorative textiles. High-strength viscose fibers can also be used in industrial products such as tire cords and conveyor belts. Viscose fiber is a widely used chemical fiber. The preparation method of viscose fiber is to extract pure ⁇ -cellulose from cellulose raw material, called pulp, and treat with caustic soda and carbon disulfide to obtain orange yellow cellulose xanthate, and then dissolve in dilute sodium hydroxide solution. In the middle, it becomes a viscous spinning dope called viscose.
- the viscose is filtered and cooked, that is, it is left at a certain temperature for about 18 to 30 hours to reduce the degree of esterification of the cellulose xanthate, and after defoaming, wet spinning is carried out.
- the coagulation bath is composed of sulfuric acid, sodium sulfate and zinc sulfate.
- the cellulose xanthate in the viscose decomposes with the sulfuric acid in the coagulation bath, and the cellulose is regenerated and precipitated.
- the obtained cellulose fiber is washed, desulfurized, bleached, After drying, it becomes viscose fiber. In the production process of viscose fiber, a large amount of exhaust gas is generated.
- the exhaust gas contains a large amount of toxic carbon disulfide, odorous hydrogen sulfide and other easily igniting and explosive gases, and there is a strong scent of snoring. Serious harm to people's physical and mental health and safety.
- the present invention provides a spray separator device having a reasonable structural design, high efficiency and energy saving, low resistance drop, and reliable performance.
- the present invention provides a spray separator device including a first casing, a second casing, a sewage cooler, a wave plate device, a square cylinder, a sewage inlet, and a sewage outlet. , heat exchange tube, chilled water outlet and chilled water inlet, vent;
- the first casing has a sewage inlet on one side, and the other side is sealedly connected to the sewage cooler;
- the second casing has a sewage outlet on one side, and the other side is sealed and connected to the wave plate assembly;
- the gas cooler is connected to the wave plate device through a square cylinder;
- the sewage cooler has a built-in heat exchange tube, and a chilled water outlet and a chilled water inlet are opened on the side, and the chilled water outlet and the chilled water inlet are connected with the heat exchange tube; the external fan unit of the spray separator device is used in the production process of the viscose fiber.
- the exhaust gas is sucked from the sewage separator inlet of the spray separator, passes through the sewage cooler, generates heat exchange, and the water vapor in the sewage, carbon disulfide, encounters chilled water below the dew point, and liquid water is formed.
- the wave plate assembly includes a wave plate assembly, and the material passes through the wave plate and is guided by the wave plate to form an S-shaped plate.
- the residual unseparated sulfur dioxide is intercepted by the wave plate wire, and the carbon disulfide material is basically completely separated, and the separated liquid material such as carbon disulfide is discharged from the sewage outlet; it is stored and handled in a safe place; the discharge port is opened below the side of the wave plate device.
- the first casing and the second casing have the same specifications and are round-day local casings; the heat exchange tubes adopt high-frequency welded finned tubes; the design greatly increases the heat exchange area and heat exchange efficiency, so that It achieves energy efficiency.
- a first manhole is defined in a side of the first casing, and a second manhole is opened in the second casing.
- a first support is embedded between the first housing and the sewage cooler, and a second support is embedded in the second housing and the wave plate assembly.
- the invention belongs to a two-in-one device, reduces manufacturing cost, has the advantages of reasonable structural design, high efficiency and energy saving, low resistance drop and reliable performance; the invention adopts a round-shaped local shell and high-frequency welding fins for replacement.
- the heat pipe greatly increases the heat exchange area and heat exchange efficiency, reduces the air pollution caused by the exhaust gas, and achieves high efficiency and energy saving, which is three times the ordinary heat exchange area.
- Figure 1 is a schematic view showing the structure of a spray separator device
- Figure 2 is a side cross-sectional view of the sewage cooler of the present invention
- Figure 3 is a view of the wave plate assembly of the present invention.
- Figure 4 is an enlarged view of the wave plate assembly B of the present invention.
- a spray separator device includes a first casing 101, a second casing 102, a sewage cooler 2, a wave plate device 4, a square cylinder 3, a sewage inlet 6, and a sewage Gas outlet 7, heat exchange tube 201, chilled water outlet 202 and chilled water inlet 203, venting port 401;
- the first casing 101 has a sewage inlet 6 on one side and a sealed connection to the sewage cooler 2 on the other side; the second casing 102 has a sewage outlet 7 on the side and a wave plate on the other side.
- the assembly 4 is sealingly connected; the sewage cooler 2 and the wave plate device 4 are sealingly connected by the square cylinder 3;
- the sewage cooler 2 has a heat exchange tube 201 built therein, a chilled water outlet 202 and a chilled water inlet (203) are opened on the side, and the chilled water outlet 202 and the chilled water inlet 203 are in communication with the heat exchange tube 201;
- the unit draws the exhaust gas from the viscose fiber production process from the sewage separator inlet 6 and passes through the sewage cooler 2 to generate heat exchange, water vapor in the sewage, carbon disulfide, and chilled water below the dew point. Form liquid water.
- the wave plate assembly 4 includes a wave plate assembly, and the material passes through the wave plate and is guided by the wave plate to form an S-shaped wind direction.
- the residual unseparated sulfur dioxide is intercepted by the wave plate wire, and the carbon disulfide material is completely separated, and the separated carbon disulfide liquid is separated.
- the object is discharged from the sewage outlet; it is stored and handled in a safe place; the discharge port 401 is opened below the side of the wave plate device 4.
- the first casing 101 and the second casing 102 are the same in size and are a round-shaped local casing, and the heat exchange tube 201 is a high-frequency welded finned tube; the design greatly increases the heat exchange area and heat exchange. Efficiency makes it energy efficient.
- a first manhole 10101 is defined in a side of the first casing 101, and a second manhole 10201 is defined in the second casing 102.
- a first support 501 is embedded between the first housing 101 and the sewage cooler 2, and a second support 502 is embedded in the second housing (102 and the wave plate assembly 4).
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A separator device, comprising a first shell (101), a second shell (102), a polluted gas cooler (2), a waved plate device (4), a square barrel (3), a polluted gas inlet (6), a polluted gas outlet (7), a heat exchange tube (201), a chilled water outlet (202), a chilled water inlet (203) and a relief outlet (401). One side of the first shell (101) is provided with the polluted gas inlet (6), and the other side of the first shell (101) is in hermetic connection with the polluted gas cooler (2). One side of the second shell (102) is provided with the polluted gas outlet (7), and the other side of the second shell (102) is in hermetic connection with the waved plate component (4). The polluted gas cooler (2) is in hermetic connection with the waved plate device (4) through the square barrel (3). The polluted gas cooler (2) is internally provided with the heat exchange tube (201), and the lateral surface of the polluted gas cooler (2) is provided with the chilled water outlet (202) and the chilled water inlet (203) that are communicated with the heat exchange tube (201). The waved plate device (4) is internally provided with the waved plate component, and the lower part of the lateral surface of the waved plate device (4) is provided with the relief outlet (401).
Description
一种喷洒分离器装置 Spray separator device
技术领域 Technical field
本发明涉及一种。 特别是涉及到纤维制造过程中的二硫化碳回收核心设备之一喷洒分离 器装置。 The invention relates to one. In particular, it relates to a spray separator device which is one of the core equipment for carbon disulfide recovery in the fiber manufacturing process.
背景技术 Background technique
粘胶纤维是最早投入工业化生产的化学纤维之一。 由于吸湿性好， 穿着舒适， 可纺性优 良， 常与棉、 毛或各种合成纤维混纺、 交织、 用于各类服装及装饰用纺织品。 高强力粘胶纤 维还可用于轮胎帘子线、 运输带等工业用品。 粘胶纤维是一种应用较广泛的化学纤维。 粘胶 纤维的制备方法， 是由纤维素原料提取出纯净的 α—纤维素称为浆粕， 用烧碱、 二硫化碳处 理， 得到橙黄色的纤维素黄原酸钠， 再溶解在稀氢氧化钠溶液中， 成为粘稠的纺丝原液， 称 为粘胶。 粘胶经过滤、 熟成， 即是在一定温度下放置约 18〜30 小时， 以降低纤维素黄原酸 酯的酯化度， 脱泡后， 进行湿法纺丝。 凝固浴是由硫酸、 硫酸钠和硫酸锌组成， 粘胶中的纤 维素黄原酸钠与凝固浴中的硫酸作用而分解， 纤维素再生而析出， 所得纤维素纤维经水洗、 脱硫、 漂白、 干燥后成为粘胶纤维。 在粘胶纤维生产过程中， 产生了大量的废气， 废气中含 有大量有毒的二硫化碳、 有异味的硫化氢及其它易着火、 易爆炸气体， 远远便有一股浓烈的 剌鼻气味扑面而来， 严重的危害着人们的身心健康和安全。 Viscose fiber is one of the first chemical fibers to be industrially produced. Because of its good hygroscopicity, comfortable wearing and excellent spinnability, it is often blended with cotton, wool or various synthetic fibers, interwoven, used in all kinds of clothing and decorative textiles. High-strength viscose fibers can also be used in industrial products such as tire cords and conveyor belts. Viscose fiber is a widely used chemical fiber. The preparation method of viscose fiber is to extract pure α-cellulose from cellulose raw material, called pulp, and treat with caustic soda and carbon disulfide to obtain orange yellow cellulose xanthate, and then dissolve in dilute sodium hydroxide solution. In the middle, it becomes a viscous spinning dope called viscose. The viscose is filtered and cooked, that is, it is left at a certain temperature for about 18 to 30 hours to reduce the degree of esterification of the cellulose xanthate, and after defoaming, wet spinning is carried out. The coagulation bath is composed of sulfuric acid, sodium sulfate and zinc sulfate. The cellulose xanthate in the viscose decomposes with the sulfuric acid in the coagulation bath, and the cellulose is regenerated and precipitated. The obtained cellulose fiber is washed, desulfurized, bleached, After drying, it becomes viscose fiber. In the production process of viscose fiber, a large amount of exhaust gas is generated. The exhaust gas contains a large amount of toxic carbon disulfide, odorous hydrogen sulfide and other easily igniting and explosive gases, and there is a strong scent of snoring. Serious harm to people's physical and mental health and safety.
发明内容 Summary of the invention
所要解决的技术问题： 针对以上问题本发明提供了一种结构设计合理、 高效节能、 阻力 降小、 性能可靠的喷洒分离器装置。 Technical Problem to be Solved: In view of the above problems, the present invention provides a spray separator device having a reasonable structural design, high efficiency and energy saving, low resistance drop, and reliable performance.
技术方案： 为了解决以上问题， 本发明提供了一种喷洒分离器装置， 包括第一壳体、 第二壳 体、 污气冷却器、 波浪板装置、 方筒体、 污气进口、 污气出口、 换热管、 冷冻水出口和冷 冻水进口、 泄放口； Technical Solution: In order to solve the above problems, the present invention provides a spray separator device including a first casing, a second casing, a sewage cooler, a wave plate device, a square cylinder, a sewage inlet, and a sewage outlet. , heat exchange tube, chilled water outlet and chilled water inlet, vent;
所述的第一壳体一侧开设污气进口， 另一侧与污气冷却器密封连接； 所述的第二壳体一 侧开设污气出口， 另一侧与波浪板组件密封连接； 污气冷却器与波浪板装置通过方筒体密 封连接； The first casing has a sewage inlet on one side, and the other side is sealedly connected to the sewage cooler; the second casing has a sewage outlet on one side, and the other side is sealed and connected to the wave plate assembly; The gas cooler is connected to the wave plate device through a square cylinder;
所述的污气冷却器内置换热管， 侧面开设冷冻水出口和冷冻水进口， 冷冻水出口和 冷冻水进口与换热管连通； 喷洒分离器装置外用风机组将粘胶纤维生产过程中的废气从喷 洒分离器污气进口吸入， 经过污气冷却器， 产生热交换， 污气中的水蒸气， 二硫化碳， 遇到低于露点的冷冻水， 将形成液态水。 The sewage cooler has a built-in heat exchange tube, and a chilled water outlet and a chilled water inlet are opened on the side, and the chilled water outlet and the chilled water inlet are connected with the heat exchange tube; the external fan unit of the spray separator device is used in the production process of the viscose fiber. The exhaust gas is sucked from the sewage separator inlet of the spray separator, passes through the sewage cooler, generates heat exchange, and the water vapor in the sewage, carbon disulfide, encounters chilled water below the dew point, and liquid water is formed.
所述的包括波浪板装置内置波浪板组件， 物料经过波浪板， 被波浪板导向， 形成 S型
风向， 残余未分离二氧化硫经过波浪板导线截流， 基本把二硫化碳物料完全分离， 分离 的二硫化碳等液态物由排污口排出； 导入安全地点存放及处理； 波浪板装置侧面下方开 设泄放口。 The wave plate assembly includes a wave plate assembly, and the material passes through the wave plate and is guided by the wave plate to form an S-shaped plate. In the wind direction, the residual unseparated sulfur dioxide is intercepted by the wave plate wire, and the carbon disulfide material is basically completely separated, and the separated liquid material such as carbon disulfide is discharged from the sewage outlet; it is stored and handled in a safe place; the discharge port is opened below the side of the wave plate device.
所述的第一壳体、第二壳体规格相同且为天圆地方壳体；所述的换热管采用高频焊接翅 片管； 此设计大幅增加了换热面积及换热效率， 使其达到了高效节能。 The first casing and the second casing have the same specifications and are round-day local casings; the heat exchange tubes adopt high-frequency welded finned tubes; the design greatly increases the heat exchange area and heat exchange efficiency, so that It achieves energy efficiency.
所述的第一壳体侧面开设有第一人孔， 第二壳体开设有第二人孔。 A first manhole is defined in a side of the first casing, and a second manhole is opened in the second casing.
所述的第一壳体与污气冷却器之间内嵌第一支撑， 第二壳体与波浪板组件内嵌第二支 撑。 A first support is embedded between the first housing and the sewage cooler, and a second support is embedded in the second housing and the wave plate assembly.
有益的效果： 本发明属于二合一设备， 降低了制造成本， 具有结构设计合理、 高效节能、 阻力降小、 性 能可靠的优点； 本发明采用了天圆地方壳体及高频焊接翅片换热管， 大幅增加了换热面 积及换热效率， 减少废气排放的空气污染， 使其达到了高效节能， 是普通换热面积的 3倍。 附图说明 Advantageous Effects: The invention belongs to a two-in-one device, reduces manufacturing cost, has the advantages of reasonable structural design, high efficiency and energy saving, low resistance drop and reliable performance; the invention adopts a round-shaped local shell and high-frequency welding fins for replacement. The heat pipe greatly increases the heat exchange area and heat exchange efficiency, reduces the air pollution caused by the exhaust gas, and achieves high efficiency and energy saving, which is three times the ordinary heat exchange area. DRAWINGS
为了更清楚地说明本发明实施例或现有技术中的技术方案， 下面将对实施例或现有技术 描述中所需要使用的附图做简单的介绍， 下面描述中的附图仅仅是本发明的一些实施例， 对 于本领域普通技术人员来讲， 在不付出创造性劳动的前提下， 还可以根据这些附图获得其他 的附图。 在附图中： In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings to be used in the embodiments or the description of the prior art will be briefly described below, and the drawings in the following description are merely the present invention. Some of the embodiments can be obtained by those skilled in the art from the drawings without any creative work. In the drawing:
图 1是喷洒分离器装置的结构示意图； Figure 1 is a schematic view showing the structure of a spray separator device;
图 2是本发明中污气冷却器侧面剖视图； Figure 2 is a side cross-sectional view of the sewage cooler of the present invention;
图 3是本发明中波浪板组件图； Figure 3 is a view of the wave plate assembly of the present invention;
图 4是本发明中波浪板组件 B放大图。 Figure 4 is an enlarged view of the wave plate assembly B of the present invention.
具体实施方式 detailed description
下面结合附图对本发明做进一步详细说明。 实施例： The invention will be further described in detail below with reference to the accompanying drawings. Example:
如图 1至 2所示， 一种喷洒分离器装置， 包括第一壳体 101、 第二壳体 102、 污气冷却器 2、 波 浪板装置 4、 方筒体 3、 污气进口 6、 污气出口 7、 换热管 201、 冷冻水出口 202和冷冻水进口 203、 泄放口 401 ; As shown in Figures 1 to 2, a spray separator device includes a first casing 101, a second casing 102, a sewage cooler 2, a wave plate device 4, a square cylinder 3, a sewage inlet 6, and a sewage Gas outlet 7, heat exchange tube 201, chilled water outlet 202 and chilled water inlet 203, venting port 401;
所述的第一壳体 101—侧开设污气进口 6， 另一侧与污气冷却器 2密封连接； 所述的第二 壳体 102—侧开设污气出口 7， 另一侧与波浪板组件 4密封连接； 污气冷却器 2与波浪板装置 4 通过方筒体 3密封连接；
所述的污气冷却器 2内置换热管 201， 侧面开设冷冻水出口 202和冷冻水进口 （203 ) ， 冷冻水出口 202和冷冻水进口 203与换热管 201连通； 喷洒分离器装置外用风机组将粘胶纤 维生产过程中的废气从喷洒分离器污气进口 6吸入， 经过污气冷却器 2， 产生热交换， 污气 中的水蒸气， 二硫化碳， 遇到低于露点的冷冻水， 将形成液态水。 The first casing 101 has a sewage inlet 6 on one side and a sealed connection to the sewage cooler 2 on the other side; the second casing 102 has a sewage outlet 7 on the side and a wave plate on the other side. The assembly 4 is sealingly connected; the sewage cooler 2 and the wave plate device 4 are sealingly connected by the square cylinder 3; The sewage cooler 2 has a heat exchange tube 201 built therein, a chilled water outlet 202 and a chilled water inlet (203) are opened on the side, and the chilled water outlet 202 and the chilled water inlet 203 are in communication with the heat exchange tube 201; The unit draws the exhaust gas from the viscose fiber production process from the sewage separator inlet 6 and passes through the sewage cooler 2 to generate heat exchange, water vapor in the sewage, carbon disulfide, and chilled water below the dew point. Form liquid water.
所述的包括波浪板装置 4内置波浪板组件， 物料经过波浪板， 被波浪板导向， 形成 S型 风向， 残余未分离二氧化硫经过波浪板导线截流， 基本把二硫化碳物料完全分离， 分离 的二硫化碳等液态物由排污口排出； 导入安全地点存放及处理；波浪板装置 4侧面下方开 设泄放口 401。 The wave plate assembly 4 includes a wave plate assembly, and the material passes through the wave plate and is guided by the wave plate to form an S-shaped wind direction. The residual unseparated sulfur dioxide is intercepted by the wave plate wire, and the carbon disulfide material is completely separated, and the separated carbon disulfide liquid is separated. The object is discharged from the sewage outlet; it is stored and handled in a safe place; the discharge port 401 is opened below the side of the wave plate device 4.
所述的第一壳体 101、 第二壳体 102规格相同且为天圆地方壳体， 所述的换热管 201采用 高频焊接翅片管； 此设计大幅增加了换热面积及换热效率， 使其达到了高效节能。 The first casing 101 and the second casing 102 are the same in size and are a round-shaped local casing, and the heat exchange tube 201 is a high-frequency welded finned tube; the design greatly increases the heat exchange area and heat exchange. Efficiency makes it energy efficient.
所述的第一壳体 101侧面开设有第一人孔 10101， 第二壳体 102开设有第二人孔 10201。 所述的第一壳体 101与污气冷却器 2之间内嵌第一支撑 501， 第二壳体（102与波浪板组件 4内嵌第二支撑 502。 A first manhole 10101 is defined in a side of the first casing 101, and a second manhole 10201 is defined in the second casing 102. A first support 501 is embedded between the first housing 101 and the sewage cooler 2, and a second support 502 is embedded in the second housing (102 and the wave plate assembly 4).
以上所述的具体实施例， 对本发明的目的、技术方案和有益效果进行了进一步详细说明， 所应理解的是， 以上所述仅为本发明的具体实施案例而已， 并不用于限定本发明的保护范围， 凡在本发明的精神和原则之内， 所做的任何修改， 等同替换、 改进等， 均应包含在本发明的 保护范围之内。
The specific embodiments of the present invention have been described in detail with reference to the preferred embodiments of the present invention. All modifications, equivalents, improvements, etc., made within the spirit and scope of the invention are intended to be included within the scope of the invention.
Claims
1、 一种喷洒分离器装置， 其特征在于： 包括第一壳体 （101)、 第二壳体 （102)、 污气冷却 器 （2) 、 波浪板装置 （4)、 方筒体 （3)、 污气进口 （6)、 污气出口 （7)、 换热管 （201) 、 冷冻水出口 （202) 和冷冻水进口 （203) 、 泄放口 （401) ； 1. A spray separator device, characterized by: including a first housing (101), a second housing (102), a waste gas cooler (2), a corrugated plate device (4), and a square cylinder (3 ), sewage inlet (6), sewage outlet (7), heat exchange tube (201), chilled water outlet (202), chilled water inlet (203), and relief port (401);
所述的第一壳体 （101) —侧开设污气进口 （6)， 另一侧与污气冷却器 （2) 密封连接； 所述的第二壳体 （102) —侧开设污气出口 （7)， 另一侧与波浪板组件 （4)密封连接； 污气 冷却器 （2) 与波浪板装置 （4) 通过方筒体 （3) 密封连接； The first housing (101) has a waste gas inlet (6) on one side, and the other side is sealed with the waste gas cooler (2); the second housing (102) has a waste gas outlet on one side. (7), the other side is sealingly connected to the corrugated plate assembly (4); the waste gas cooler (2) and the corrugated plate device (4) are sealingly connected through the square cylinder (3);
所述的污气冷却器 （2) 内置换热管 （201) ， 侧面开设冷冻水出口 （202) 和冷冻水 进口 （203) ， 冷冻水出口 （202) 和冷冻水进口 （203) 与换热管 （201) 连通； The waste gas cooler (2) has a heat exchange pipe (201) inside, and a chilled water outlet (202) and a chilled water inlet (203) are provided on the side. The chilled water outlet (202) and the chilled water inlet (203) are connected to the heat exchanger. tube (201) connected;
所述的包括波浪板装置 （4) 内置波浪板组件， 侧面下方开设泄放口 （401) 。 The described device includes a corrugated plate device (4) with a built-in corrugated plate assembly, and a relief port (401) at the bottom of the side.
2、 根据权利要求 1所述的一种喷洒分离器装置， 其特征在于： 所述的第一壳体 （101)、 第二 壳体 （102) 规格相同且为天圆地方壳体。 2. A spray separator device according to claim 1, characterized in that: the first housing (101) and the second housing (102) have the same specifications and are round housings.
3、 根据权利要求 1所述的一种喷洒分离器装置， 其特征在于： 所述的换热管 （201) 采用高 频焊接翅片管。 3. A spray separator device according to claim 1, characterized in that: the heat exchange tube (201) adopts high-frequency welded fin tube.
4、 根据权利要求 1所述的一种喷洒分离器装置， 其特征在于： 所述的第一壳体（101)侧面开 设有第一人孔 （10101)， 第二壳体 （102) 开设有第二人孔 （10201)。 4. A spray separator device according to claim 1, characterized in that: the first housing (101) is provided with a first manhole (10101) on the side, and the second housing (102) is provided with a first manhole (10101). Second manhole (10201).
5、 根据权利要求 1所述的一种喷洒分离器装置， 其特征在于： 所述的第一壳体（101)与污气 冷却器 （2) 之间内嵌入第一支撑（501)， 第二壳体（102) 与波浪板组件（4) 内嵌入第二 支撑 （502)。
5. A spray separator device according to claim 1, characterized in that: a first support (501) is embedded between the first housing (101) and the waste gas cooler (2), The second support (502) is embedded in the second shell (102) and the corrugated plate assembly (4).
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410002592.0 | 2014-01-04 | ||
| CN201410002592.0A CN103752126A (en) | 2014-01-04 | 2014-01-04 | Spraying separator device |
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| Publication Number | Publication Date |
|---|---|
| WO2015101053A1 true WO2015101053A1 (en) | 2015-07-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN2014/084997 WO2015101053A1 (en) | 2014-01-04 | 2014-08-22 | Spraying separator device |
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| WO (1) | WO2015101053A1 (en) |
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| CN103752126A (en) * | 2014-01-04 | 2014-04-30 | 江苏民生特种设备集团有限公司 | Spraying separator device |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101439235A (en) * | 2007-11-22 | 2009-05-27 | 东京毅力科创株式会社 | Gas-liquid separating device |
| CN103170187A (en) * | 2013-03-22 | 2013-06-26 | 无锡宏盛换热器制造股份有限公司 | Cooler for integrated water separation device |
| CN103752126A (en) * | 2014-01-04 | 2014-04-30 | 江苏民生特种设备集团有限公司 | Spraying separator device |
| CN203694861U (en) * | 2014-01-04 | 2014-07-09 | 江苏民生特种设备集团有限公司 | Spraying separator |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201300030Y (en) * | 2008-10-31 | 2009-09-02 | 刘振海 | Improved air cooling and water eliminating device |
| CN102210939A (en) * | 2011-06-09 | 2011-10-12 | 浙江省环境工程有限公司 | Method and device for treating nitrochlorobenzene waste gas |
| CN202715264U (en) * | 2012-06-20 | 2013-02-06 | 杭州奥通科技有限公司 | Viscose fibre waste gas condensing device |
-
2014
- 2014-01-04 CN CN201410002592.0A patent/CN103752126A/en active Pending
- 2014-08-22 WO PCT/CN2014/084997 patent/WO2015101053A1/en active Application Filing
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101439235A (en) * | 2007-11-22 | 2009-05-27 | 东京毅力科创株式会社 | Gas-liquid separating device |
| CN103170187A (en) * | 2013-03-22 | 2013-06-26 | 无锡宏盛换热器制造股份有限公司 | Cooler for integrated water separation device |
| CN103752126A (en) * | 2014-01-04 | 2014-04-30 | 江苏民生特种设备集团有限公司 | Spraying separator device |
| CN203694861U (en) * | 2014-01-04 | 2014-07-09 | 江苏民生特种设备集团有限公司 | Spraying separator |
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