CN115626726A - Industrial impurity removal system and method for jiale musk chlorobenzene rear-stage waste liquid - Google Patents
Industrial impurity removal system and method for jiale musk chlorobenzene rear-stage waste liquid Download PDFInfo
- Publication number
- CN115626726A CN115626726A CN202211197549.5A CN202211197549A CN115626726A CN 115626726 A CN115626726 A CN 115626726A CN 202211197549 A CN202211197549 A CN 202211197549A CN 115626726 A CN115626726 A CN 115626726A
- Authority
- CN
- China
- Prior art keywords
- chlorobenzene
- waste liquid
- top surface
- cover
- impurity removal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 title claims abstract description 111
- 239000007788 liquid Substances 0.000 title claims abstract description 43
- 239000012535 impurity Substances 0.000 title claims abstract description 34
- 239000002699 waste material Substances 0.000 title claims abstract description 29
- 241000402754 Erythranthe moschata Species 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims description 18
- 230000007246 mechanism Effects 0.000 claims abstract description 66
- 238000004140 cleaning Methods 0.000 claims abstract description 43
- 238000003756 stirring Methods 0.000 claims abstract description 40
- 230000005540 biological transmission Effects 0.000 claims abstract description 25
- 238000007790 scraping Methods 0.000 claims abstract description 13
- 238000007789 sealing Methods 0.000 claims description 31
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- RZWHKKIXMPLQEM-UHFFFAOYSA-N 1-chloropropan-1-ol Chemical compound CCC(O)Cl RZWHKKIXMPLQEM-UHFFFAOYSA-N 0.000 claims description 14
- 239000000243 solution Substances 0.000 claims description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 12
- 239000000463 material Substances 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 238000004817 gas chromatography Methods 0.000 claims description 6
- PQNFLJBBNBOBRQ-UHFFFAOYSA-N indane Chemical compound C1=CC=C2CCCC2=C1 PQNFLJBBNBOBRQ-UHFFFAOYSA-N 0.000 claims description 6
- 230000001680 brushing effect Effects 0.000 claims description 5
- 238000005406 washing Methods 0.000 claims description 5
- 239000002351 wastewater Substances 0.000 claims description 5
- 239000012043 crude product Substances 0.000 claims description 4
- NKDDWNXOKDWJAK-UHFFFAOYSA-N dimethoxymethane Chemical compound COCOC NKDDWNXOKDWJAK-UHFFFAOYSA-N 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 claims description 3
- 238000006386 neutralization reaction Methods 0.000 claims description 3
- 229920000642 polymer Polymers 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims 3
- 235000017491 Bambusa tulda Nutrition 0.000 claims 3
- 241001330002 Bambuseae Species 0.000 claims 3
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims 3
- 230000006978 adaptation Effects 0.000 claims 3
- 239000011425 bamboo Substances 0.000 claims 3
- 238000007599 discharging Methods 0.000 claims 3
- 239000012295 chemical reaction liquid Substances 0.000 claims 1
- 238000001816 cooling Methods 0.000 claims 1
- 238000001514 detection method Methods 0.000 claims 1
- 238000007865 diluting Methods 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 239000011344 liquid material Substances 0.000 abstract description 4
- 238000013461 design Methods 0.000 abstract description 3
- 230000007812 deficiency Effects 0.000 abstract description 2
- 238000005457 optimization Methods 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 239000003513 alkali Substances 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 239000008346 aqueous phase Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- ONKNPOPIGWHAQC-UHFFFAOYSA-N galaxolide Chemical compound C1OCC(C)C2=C1C=C1C(C)(C)C(C)C(C)(C)C1=C2 ONKNPOPIGWHAQC-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000005923 long-lasting effect Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000003913 materials processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
本发明公开了一种佳乐麝香氯苯后段废液的工业除杂系统,包括釜体主体、顶盘组件、底盘和防旋下料机构,所述顶盘组件、釜体主体、底盘和防旋下料机构从上至下依次密封套装,所述顶盘组件底面的中部轴承套接有传动轴,所述传动轴的外表面套装有搅拌机构,所述搅拌机构外表面的底端套装有清刷机构,所述底盘顶面的中部设有刮料机构,所述底盘的底面设有支撑柱。本发明克服了现有技术的不足,设计合理,结构紧凑,利用搅拌转动方向的相向设置,让釜内的液体物料能够进行上下翻转式的搅拌,并且根据出料端的优化,让分层导出液体出现旋涡的情况得到了减弱,具有较高的社会使用价值和应用前景。
The invention discloses an industrial impurity removal system for the rear stage waste liquid of Jiale musk chlorobenzene. The anti-rotation feeding mechanism is sealed and fitted sequentially from top to bottom. The middle bearing on the bottom surface of the top plate assembly is sleeved with a transmission shaft. The outer surface of the transmission shaft is fitted with a stirring mechanism. The bottom end of the outer surface of the stirring mechanism is fitted There is a cleaning mechanism, the middle part of the top surface of the chassis is provided with a scraping mechanism, and the bottom surface of the chassis is provided with a support column. The invention overcomes the deficiencies of the prior art, and has a reasonable design and a compact structure. The liquid material in the kettle can be stirred up and down by using the opposite setting of the stirring rotation direction, and the liquid can be exported layer by layer according to the optimization of the discharge end. The appearance of the vortex has been weakened, and has high social use value and application prospect.
Description
技术领域technical field
本发明涉及佳乐麝香氯苯废液除杂技术领域,尤其涉及一种佳乐麝香氯苯后段废液的工业除杂系统及方法。The invention relates to the technical field of impurity removal of Jiale musk chlorobenzene waste liquid, in particular to an industrial impurity removal system and method for Jiale musk chlorobenzene waste liquid at the rear stage.
背景技术Background technique
佳乐麝香是一种合成式麝香,其分子量为258.4,沸点129℃ (107Pa),化学名称为1,3,4,6,7,8-六氢-4,6,6,7,8,8-六甲基环五-γ-2-苯并吡喃,能够挥发强烈而持久的麝香香气,并在挥发的过程中伴有木香香气,广泛用作化妆品、皂用香精等行业进行辅助配香。Jiale musk is a synthetic musk with a molecular weight of 258.4, a boiling point of 129°C (107Pa), and a chemical name of 1,3,4,6,7,8-hexahydro-4,6,6,7,8, 8-Hexamethylcyclopenta-γ-2-benzopyran can volatilize a strong and long-lasting musk aroma, accompanied by woody aroma during the volatilization process, and is widely used as an auxiliary in cosmetics, soap essence and other industries With fragrance.
在佳乐麝香的生产后端,会产生一定量的氯苯塔底废液,而氯苯塔底废液氯丙醇夹带较多,使得氯苯回收难度大,氯苯纯品回收率低,大量的杂质和氯苯重合,回收后氯苯纯度低的问题,并且反应釜在对氯苯进行回收处理的过程中,其内部的杂质会留存于反应釜的内部,并且在进行分层操作的时候容易出现分层下料造成旋涡过大,直接影响分层下料的情况,为此,我们提出了采用水洗以及碱洗的操作方式,并且针对下料分层容易受到旋涡影响的情况进行优化的除杂系统。At the back end of the production of Jiale musk, a certain amount of chlorobenzene tower bottom waste liquid will be produced, and the chlorobenzene tower bottom waste liquid contains more chloropropanol, which makes the recovery of chlorobenzene difficult, and the recovery rate of pure chlorobenzene is low. A large number of impurities overlap with chlorobenzene, the problem of low purity of chlorobenzene after recovery, and during the recovery process of p-chlorobenzene in the reactor, the internal impurities will remain in the reactor, and during the layering operation Sometimes it is easy to cause the vortex to be too large due to layered feeding, which directly affects the layered feeding. For this reason, we propose the operation method of water washing and alkali cleaning, and optimize the situation that the feeding layer is easily affected by the vortex. of impurity removal system.
于是,发明人有鉴于此,秉持多年该相关行业丰富的设计开发及实际制作的经验,针对现有的结构及缺失予以研究改良,提供一种佳乐麝香氯苯后段废液的工业除杂系统及方法,以期达到更具有实用价值的目的。Therefore, in view of this, the inventor has been adhering to many years of rich experience in design, development and actual production in this related industry, researched and improved the existing structure and defects, and provided an industrial impurity removal for the waste liquid of chlorobenzene in the back stage of Jiale musk System and method, in order to achieve the purpose of more practical value.
发明内容Contents of the invention
为了解决上述背景技术中提到的问题,本发明提供一种佳乐麝香氯苯后段废液的工业除杂系统及方法。In order to solve the problems mentioned in the above-mentioned background technology, the present invention provides an industrial impurity removal system and method for the rear-stage waste liquid of chlorobenzene of carole musk.
为了实现上述目的,本发明采用了如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
一种佳乐麝香氯苯后段废液的工业除杂系统及方法,包括釜体主体、顶盘组件、底盘和防旋下料机构,所述顶盘组件、釜体主体、底盘和防旋下料机构从上至下依次密封套装,所述顶盘组件底面的中部轴承套接有传动轴,所述传动轴的外表面套装有搅拌机构,所述搅拌机构外表面的底端套装有清刷机构,所述底盘顶面的中部设有刮料机构,所述底盘的底面设有支撑柱。An industrial impurity removal system and method for the rear-stage waste liquid of Jiale musk chlorobenzene, including the main body of the kettle body, the top plate assembly, the chassis and the anti-rotation feeding mechanism, the top plate assembly, the main body of the kettle body, the chassis and the anti-rotation The unloading mechanism is sealed sequentially from top to bottom. The middle bearing on the bottom surface of the top plate assembly is sleeved with a drive shaft. The outer surface of the drive shaft is set with a stirring mechanism. A brushing mechanism, a scraping mechanism is provided in the middle of the top surface of the chassis, and a support column is provided on the bottom surface of the chassis.
优选地,所述顶盘组件包括顶盖盘,所述顶盖盘的底面与釜体主体的顶面密封套装,所述顶盖盘的顶面套装有驱动电机,所述驱动电机输出端的底端与传动轴的顶端轴承套装,所述顶盖盘顶面的右侧连通设有第一进料管,所述顶盖盘顶面的右侧连通设有第二进料管,所述顶盖盘顶面的左端连通设有主投料管。Preferably, the top plate assembly includes a top cover plate, the bottom surface of the top cover plate is sealed with the top surface of the kettle body body, the top surface of the top cover plate is set with a drive motor, and the bottom of the output end of the drive motor end and the top bearing of the transmission shaft, the right side of the top surface of the top cover plate is connected with a first feed pipe, and the right side of the top cover plate is connected with a second feed pipe, and the top surface of the top cover plate is connected with a second feed pipe. The left end of the top surface of the cover plate is communicated with a main feeding pipe.
优选地,所述防旋下料机构包括定位套筒,所述定位套筒的顶面与底盘的底面中部连通设置,所述定位套筒的内腔密封套设有下料管筒,所述下料管筒的底端连通设有调节筒,所述调节筒的底面连通设有调节块,所述调节块的底面轴承套设有连通管,所述下料管筒的顶面套设有防旋罩,所述防旋罩的顶面套设有密封顶板。Preferably, the anti-rotation blanking mechanism includes a positioning sleeve, the top surface of the positioning sleeve communicates with the middle part of the bottom surface of the chassis, and the inner cavity sealing sleeve of the positioning sleeve is provided with a blanking tube. The bottom of the feeding tube is connected with an adjusting tube, the bottom of the adjusting tube is connected with an adjusting block, the bottom bearing sleeve of the adjusting block is provided with a connecting pipe, and the top surface of the feeding tube is sleeved with a The anti-rotation cover, the top surface of the anti-rotation cover is covered with a sealing top plate.
优选地,所述搅拌机构包括螺旋搅拌片和套装柱,所述螺旋搅拌片的内腔与传动轴的外表面固定套设,所述套装柱套装于螺旋搅拌片的外表面。Preferably, the stirring mechanism includes a helical stirring piece and a sleeve, the inner cavity of the helical stirring piece is fixedly sleeved with the outer surface of the transmission shaft, and the sleeved column is sleeved on the outer surface of the helical stirring piece.
优选地,所述清刷机构包括拼接座,所述拼接座的顶端与传动轴的底端固定套设,所述拼接座外表面的底端周向均匀设有支撑杆,所述支撑杆的端部设有清刷板,所述拼接座外表面的顶端周向均匀设有平衡杆,所述平衡杆的外侧端部与清刷板的内侧面连接。Preferably, the cleaning mechanism includes a splicing seat, the top of the splicing seat is fixedly sleeved with the bottom end of the transmission shaft, and the bottom end of the outer surface of the splicing seat is evenly provided with support rods in the circumferential direction. A cleaning board is provided at the end, and a balance bar is evenly provided on the top of the outer surface of the splicing seat in the circumferential direction, and the outer end of the balance bar is connected with the inner surface of the cleaning board.
优选地,所述刮料机构包括支撑座,所述支撑座的底面与底盘内腔底面的中部连接,所述支撑座的顶面中部轴承套设有连接柱,所述连接柱的外表面设有延伸杆,所述延伸杆的底面设有刮料推动板。Preferably, the scraping mechanism includes a support seat, the bottom surface of the support seat is connected to the middle part of the bottom surface of the inner cavity of the chassis, the bearing sleeve in the middle part of the top surface of the support seat is provided with a connecting column, and the outer surface of the connecting column is provided There is an extension rod, and the bottom surface of the extension rod is provided with a scraper pushing plate.
优选地,所述螺旋搅拌片的内腔开设有套装孔,所述套装孔的大小和形状与传动轴的大小和形状相适配,所述拼接座的底端与连接柱的顶面固定套设,所述支撑座的周向表面开设有下料口,所述支撑座内腔的顶面开设有密封槽,所述密封槽的大小和形状与密封顶板顶面的大小和形状相适配。Preferably, the inner cavity of the spiral stirring blade is provided with a fitting hole, the size and shape of the fitting hole are adapted to the size and shape of the transmission shaft, and the bottom end of the splicing seat is fixed with the top surface of the connecting column. It is provided that a feeding port is provided on the circumferential surface of the support seat, and a sealing groove is provided on the top surface of the inner cavity of the support seat, and the size and shape of the sealing groove match the size and shape of the top surface of the sealing top plate. .
优选地,所述定位套筒的内腔侧壁设有密封限位环,所述密封限位环的内径大小和形状与下料管筒外表面的大小和形状相适配,所述密封顶板的外表面套装有顶部密封圈,所述调节筒的顶面设有位于下料管筒外侧的底部密封环,所述密封顶板顶面的中部连通有导液管。Preferably, the side wall of the inner cavity of the positioning sleeve is provided with a sealing limit ring, the size and shape of the inner diameter of the sealing limit ring are adapted to the size and shape of the outer surface of the feeding tube, and the sealing top plate A top sealing ring is set on the outer surface of the adjustment cylinder, a bottom sealing ring located outside the feeding tube is provided on the top surface of the regulating cylinder, and a catheter is connected to the middle of the top surface of the sealing top plate.
优选地,所述清刷板的数量为三个,三个清刷板周向均分设在釜体主体的内腔,所述清刷板的外表面设有清理刷,所述清理刷的端部与釜体主体的内部接触。Preferably, the number of the cleaning boards is three, and the three cleaning boards are arranged in the inner cavity of the kettle body body in a circumferential direction, and the outer surface of the cleaning boards is provided with cleaning brushes, and the ends of the cleaning brushes are connected to the The internal contact of the main body of the kettle.
优选地,所述刮料推动板的底端与底盘的内腔底面留设有空隙,所述空隙留设的大小可随支撑座和连接柱套设的位置进行调整。Preferably, there is a gap between the bottom end of the scraper pushing plate and the bottom surface of the inner cavity of the chassis, and the size of the gap can be adjusted according to the positions of the support seat and the connecting column.
一种佳乐麝香氯苯后段废液的工业除杂方法,包括以下步骤:A kind of industrial impurity removal method of Jiale musk chlorobenzene rear section waste liquid, comprises the following steps:
S1:通过主投料管向釜体主体中加入3000kg氯苯塔底废液(氯苯80%、氯丙醇10%,甲缩醛和氯丙醇聚合物8%,茚满2%),开启驱动电机,使得驱动电机的输出轴能够间接带动套装柱、清刷板和刮料推动板进行搅拌,将第一进料管与外部的蒸汽供应管道连通,并且进行蒸汽输入加热,将釜内温度升到60-90℃;S1: Add 3000kg chlorobenzene tower bottom waste liquid (80% chlorobenzene, 10% chloropropanol, 8% methylal and chloropropanol polymer, 2% indane) to the main body of the kettle body through the main feeding pipe, and start Drive the motor, so that the output shaft of the drive motor can indirectly drive the set column, the cleaning plate and the scraper pushing plate to stir, connect the first feed pipe with the external steam supply pipe, and carry out steam input heating to reduce the temperature in the kettle. Rise to 60-90°C;
S2:将第二进料管与外部管路连通,并且通过第二进料管向釜体主体的内部缓慢匀速滴加120-200kg浓度98%的硫酸,保证釜体主体的内部不剧烈沸腾,需要在2-3小时内滴加结束;S2: Connect the second feed pipe to the external pipeline, and slowly and uniformly drop 120-200 kg of sulfuric acid with a concentration of 98% to the interior of the kettle body through the second feed pipe to ensure that the interior of the kettle body does not boil violently. It needs to be added dropwise within 2-3 hours;
S3:关闭第一进料管的蒸汽输入,使得釜体主体的内部自然降温至40℃,通过第二进料管向釜体主体的内部加入纯水400kg进行水洗(将部分未参与反应的硫酸稀释),再进行搅拌1小时,而后静置1小时,混合液在釜体主体的内部进行自然分层,将下层酸水通过防旋下料机构排出至外部废水槽;S3: Turn off the steam input of the first feeding pipe, so that the inside of the kettle body is naturally cooled to 40°C, and add 400kg of pure water to the inside of the kettle body through the second feeding pipe for washing (remove part of the unreacted sulfuric acid dilute), then stirred for 1 hour, and then stood still for 1 hour, the mixed solution was naturally layered inside the main body of the kettle body, and the acid water in the lower layer was discharged to the external waste water tank through the anti-rotation feeding mechanism;
S4:将釜体主体内部上层得到的氯苯相留在釜体主体的内部,并且通过第二进料管加入5%的氢氧化钠溶液400kg(和硫酸进行中和反应,使反应液呈碱性),搅拌1小时,静置1小时自然分层,再通过防旋下料机构放出下层碱水相,即可得到处理后的氯苯粗品溶液,经过气相色谱检测氯丙醇杂质峰≤1%,氯苯含量≥90%。S4: Leave the chlorobenzene phase obtained in the upper layer of the kettle body inside the kettle body, and add 5% sodium hydroxide solution 400kg through the second feed pipe (neutralization reaction with sulfuric acid to make the reaction solution alkaline nature), stirring for 1 hour, standing for 1 hour to separate naturally, and then release the lower alkali aqueous phase through the anti-rotation feeding mechanism to obtain the treated crude chlorobenzene solution. The impurity peak of chloropropanol is detected by gas chromatography ≤ 1 %, chlorobenzene content ≥ 90%.
与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:
1、首先,通过清刷机构和刮料机构的设置,能够对釜体主体和底盘的内壁进行清洁处理,避免液体物料在反应处理的过程中出现的杂质堆积在釜体主体和底盘的内壁上,导致后期无法进行清理的情况出现,并且根据套装柱和刮料推动板的设置形状,可以将釜体主体内部的液体物料进行上下翻动搅拌处理。1. First of all, through the setting of the cleaning mechanism and the scraping mechanism, the inner wall of the main body of the kettle body and the chassis can be cleaned, so as to avoid the accumulation of impurities that appear in the reaction process of the liquid material on the inner wall of the main body of the kettle body and the chassis , resulting in the situation that it is impossible to clean up later, and according to the setting shape of the set column and the scraping push plate, the liquid material inside the main body of the kettle body can be stirred up and down.
2、其次,通过防旋下料机构的设置,利用定位套筒和调节筒之间的螺纹套接方式,让防旋罩的使用高度相对于定位套筒进行调整处理,避免在釜体主体的内部进行上下层液体分离排放的时候出现过大的旋涡,使得可用产物的留置不会轻易流失。2. Secondly, through the setting of the anti-rotation blanking mechanism, the use of the screw connection method between the positioning sleeve and the adjustment cylinder is used to adjust the use height of the anti-rotation cover relative to the positioning sleeve, so as to avoid the When the upper and lower layers of the liquid are separated and discharged inside, an excessive vortex appears, so that the retention of available products will not be easily lost.
综上,本发明克服了现有技术的不足,设计合理,结构紧凑,利用搅拌转动方向的相向设置,让釜内的液体物料能够进行上下翻转式的搅拌,并且根据出料端的优化,让分层导出液体出现旋涡的情况得到了减弱,具有较高的社会使用价值和应用前景。In summary, the present invention overcomes the deficiencies of the prior art, and has a reasonable design and a compact structure. By using the opposite setting of the stirring rotation direction, the liquid material in the kettle can be stirred up and down, and according to the optimization of the discharge end, the split The situation of the vortex in the liquid derived from the layer has been weakened, and has high social use value and application prospect.
附图说明Description of 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作简单地介绍,显而易见地,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。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following will briefly introduce the drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only These are some embodiments of the present invention. Those skilled in the art can also obtain other drawings based on these drawings without creative work.
图1为本发明的整体结构爆炸示意图。Fig. 1 is an exploded schematic view of the overall structure of the present invention.
图2为本发明的除杂流程示意图。Fig. 2 is a schematic diagram of the impurity removal process of the present invention.
图3为本发明的整体外观结构示意图。Fig. 3 is a schematic diagram of the overall appearance and structure of the present invention.
图4为本发明中底盘的结构示意图。Fig. 4 is a structural schematic diagram of the chassis of the present invention.
图5为本发明中清刷机构的结构示意图。Fig. 5 is a structural schematic diagram of the cleaning mechanism in the present invention.
图6为本发明中搅拌机构的结构示意图。Fig. 6 is a structural schematic diagram of the stirring mechanism in the present invention.
图7为本发明中刮料机构的结构示意图。Fig. 7 is a structural schematic diagram of the scraping mechanism in the present invention.
图8为本发明中防旋下料机构的开启阶段结构示意图。Fig. 8 is a structural schematic diagram of the opening stage of the anti-rotation blanking mechanism in the present invention.
图9为本发明中防旋下料机构的关闭阶段结构示意图。Fig. 9 is a structural schematic diagram of the closing stage of the anti-rotation blanking mechanism in the present invention.
图10为本发明中防旋下料机构的结构爆炸示意图。Fig. 10 is a schematic exploded view of the structure of the anti-rotation blanking mechanism in the present invention.
图中:1、釜体主体;2、顶盘组件;201、顶盖盘;202、驱动电机;203、第一进料管;204、第二进料管;205、主投料管;3、底盘;301、支撑柱;4、防旋下料机构;41、定位套筒;42、下料管筒;43、调节筒;433、底部密封环;44、调节块;45、连通管;46、防旋罩;47、密封顶板;471、导液管;5、传动轴;6、搅拌机构;61、螺旋搅拌片;62、套装柱;7、清刷机构;71、拼接座;72、支撑杆;73、平衡杆;74、清刷板;8、刮料机构;81、支撑座;82、连接柱;83、延伸杆;84、刮料推动板。In the figure: 1, kettle body main body; 2, top plate assembly; 201, top cover plate; 202, drive motor; 203, first feed pipe; 204, second feed pipe; 205, main feed pipe; 3, Chassis; 301, support column; 4, anti-rotation blanking mechanism; 41, positioning sleeve; 42, blanking tube; 43, adjusting cylinder; 433, bottom sealing ring; 44, adjusting block; 45, connecting pipe; 46 , anti-rotation cover; 47, sealing top plate; 471, catheter; 5, transmission shaft; 6, stirring mechanism; 61, spiral stirring plate; 62, set column; 7, cleaning mechanism; Support rod; 73, balance bar; 74, cleaning plate; 8, scraping mechanism; 81, support seat; 82, connecting column; 83, extension rod;
具体实施方式Detailed ways
为使本发明实施例的目的、技术方案和优点更加清楚,下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments It is a part of embodiments of the present invention, but not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
实施例1Example 1
参照图1、图3-8和图10,一种佳乐麝香氯苯后段废液的工业除杂系统及方法,包括釜体主体1、顶盘组件2、底盘3和防旋下料机构4,顶盘组件2、釜体主体1、底盘3和防旋下料机构4从上至下依次密封套装,让釜体主体1的内腔形成密闭的空间,方便进行原料的搅拌和静置处理,顶盘组件2底面的中部轴承套接有传动轴5,传动轴5可以先与驱动电机202输出轴的底端进行固定式的轴承套接,让驱动电机202的输出轴带动传动轴5进行转动,传动轴5的外表面固定套装有搅拌机构6,搅拌机构6外表面的底端固定套装有清刷机构7,底盘3顶面的中部固定栓接设有刮料机构8,底盘3的底面固定栓接设有支撑柱301。Referring to Figure 1, Figures 3-8 and Figure 10, an industrial impurity removal system and method for the rear-stage waste liquid of chlorobenzene of Jiale musk, including the main body of the
具体的,顶盘组件2包括顶盖盘201,顶盖盘201的底面与釜体主体1的顶面密封套装,顶盖盘201的顶面套装有驱动电机202,驱动电机202输出端的底端与传动轴5的顶端轴承套装,顶盖盘201顶面的右侧连通设有第一进料管203,顶盖盘201顶面的右侧连通设有第二进料管204,顶盖盘201顶面的左端连通设有主投料管205,通过顶盘组件2的设置,能够为釜体主体1的内部组件提供驱动源,并且能够为釜体主体1的顶面提供密封的作用,并且让物料从第一进料管203、第二进料管204和主投料管205导入釜体主体1的内部进行搅拌和静置处理。Specifically, the
具体的,防旋下料机构4包括定位套筒41,定位套筒41的顶面与底盘3的底面中部连通设置,定位套筒41的内腔密封套设有下料管筒42,下料管筒42的底端连通设有调节筒43,调节筒43的底面连通设有调节块44,调节块44的底面轴承套设有连通管45,下料管筒42的顶面套设有防旋罩46,防旋罩46的顶面套设有密封顶板47,通过防旋下料机构4的设置,让防旋下料机构4的内部组件能够针对物料通过底盘3与防旋下料机构4之间的连通进行下料的过程中,让下料时的旋涡情况得到减缓,避免前期静置分层的液面出现混合的情况,可以让分层下料的效率提升。Specifically, the
具体的,搅拌机构6包括螺旋搅拌片61和套装柱62,螺旋搅拌片61的内腔与传动轴5的外表面固定套设,套装柱62套装于螺旋搅拌片61的外表面,通过搅拌机构6的设置,能够在驱动电机202的输出轴带动传动轴5进行转动的情况下,让螺旋搅拌片61跟随传动轴5同步进行转动,使得套装柱62能够对釜体主体1内部的液体进行搅拌处理。Specifically, the
具体的,清刷机构7包括拼接座71,拼接座71的顶端与传动轴5的底端固定套设,拼接座71外表面的底端周向均匀设有支撑杆72,支撑杆72的端部设有清刷板74,拼接座71外表面的顶端周向均匀设有平衡杆73,平衡杆73的外侧端部与清刷板74的内侧面连接,通过清刷机构7的内部组件设置,能够在清刷板74的外表面设置清理刷,清理刷的情况为扇面状,可以直接固定在清刷板74的外表面,方便对釜体主体1的内腔侧壁进行清刷操作,并且可以进行定期的更换处理。Specifically, the cleaning mechanism 7 includes a
具体的,刮料机构8包括支撑座81,支撑座81的底面与底盘3内腔底面的中部连接,支撑座81的顶面中部轴承套设有连接柱82,连接柱82的外表面设有延伸杆83,延伸杆83的底面设有刮料推动板84,利用刮料机构8的内部组件设置,能够起到存在于底盘3内部的液体起到搅动的作用,并且可以避免杂质留置在底盘3内腔的底面上,让刮料推动板84与底盘3内腔底面附着的杂质进行接触可以起到清除的作用。Specifically, the
具体的,螺旋搅拌片61的内腔开设有套装孔,套装孔的大小和形状与传动轴5的大小和形状相适配,拼接座71的底端与连接柱82的顶面固定套设,支撑座81的周向表面开设有下料口,支撑座81内腔的顶面开设有密封槽,密封槽的大小和形状与密封顶板47顶面的大小和形状相适配,套装孔的开设能够让螺旋搅拌片61套装在传动轴5的外表面,拼接座71和连接柱82的套设可以采用固定套接的方式安装,而连接柱82与支撑座81之间的套装是采用内嵌槽的形式进行固定,方便安装操作,下料口的开设配合防旋下料机构4的内部组件,让液体下料的过程中,能够起到一定的阻挡作用,避免出现下料旋涡过大的情况。Specifically, the inner cavity of the
具体的,定位套筒41的内腔侧壁设有密封限位环,密封限位环的内径大小和形状与下料管筒42外表面的大小和形状相适配,密封顶板47的外表面套装有顶部密封圈,调节筒43的顶面设有位于下料管筒42外侧的底部密封环433,密封顶板47顶面的中部连通有导液管471,密封限位环的设置以及顶部密封圈的设置,能够让防旋下料机构4的内部组件在进行运动的时候,让防旋下料机构4和底盘3之间的连接密封,避免液体从底盘3和定位套筒41之间的连接点位以及防旋下料机构4的内部组件拼接间隙流出。Specifically, the inner cavity side wall of the
具体的,清刷板74的数量为三个,三个清刷板74周向均分设在釜体主体1的内腔,清刷板74的外表面设有清理刷,清理刷的端部与釜体主体1的内部接触,清刷板74的设置为角度间隔120度,可以最大限度的为釜体主体1的内腔侧壁配合清理刷进行清洁操作,清理刷的外表面设有刷毛,其内表面可以与清刷板74的外表面进行紧密的贴合,利用螺栓进行两者的安装固定,清理刷的轻装和大小需要与清刷板74的形状和大小相适配。Concrete, the quantity of cleaning
具体的,刮料推动板84的底端与底盘3的内腔底面留设有空隙,空隙留设的大小可随支撑座81和连接柱82套设的位置进行调整,刮料推动板84底端所留设的空隙避免刮料推动板84与底盘3的内腔底面进行直接的接触,避免在转动的时候形成硬碰撞,避免了刮料推动板84和底盘3的损坏。Specifically, there is a gap between the bottom of the
实施例2Example 2
参照图9,本实施例与实施例1的区别在于,定位套筒41和下料管筒42之间的套装位置可以进行调整,根据调节筒43外表面以及定位套筒41内部侧壁底端所开设的螺纹对应,可以通过旋转的方式进行调整,让密封顶板47的顶面与支撑座81的内腔顶面进行分离,让导液管471的顶面高度与底盘3内腔底面的高度相适配,让釜体主体1内部的料液能够通过导液管471直接的排出,无需进过防旋罩46,使得防旋下料机构4可以进行防旋程序的开启和关闭操作,该类的改善可以在釜体主体1无需进行分层排放物料的时候,避免防旋下料机构4的内部组件干涉造成下料速度的减缓。Referring to Fig. 9, the difference between this embodiment and
其他未描述结构参照实施例1。Refer to Example 1 for other undescribed structures.
工作原理:本发明中,首先通过外部泵送,将氯苯塔底废液从主投料管205导入釜体主体1的内部,然后开启驱动电机202,使得驱动电机202的输出轴能够带动传动轴5进行转动,从而让传动轴5带动套装柱62、清刷板74和刮料推动板84进行同步同向转动,并且将加热蒸汽通过第一进料管203导入釜体主体1的内部,使得釜体主体1内部的温度能够达到60-90℃,使得釜体主体1的内部能够进行搅拌和蒸汽加热处理,然后再通过第二进料管204将硫酸滴加在釜体主体1的内部,保证釜体主体1的内部不会剧烈沸腾,滴加硫酸的时间需控制在2-3小时之内,随后关闭加热蒸汽的输入,让釜体主体1的内部温度控制在40℃,再通过第二进料管204向釜体主体1的内部加入纯水进行水洗操作,并且同步开启搅拌,搅拌时间控制在1小时,搅拌结束之后需要静置釜体主体1内部的液体1小时,使得釜体主体1内部的混合液能够自然分层明显,将釜体主体1内部下层的废水通过防旋下料机构4直接导出,在导出废水的过程中,需要让防旋罩46升起,为排液起到防旋的作用,釜体主体1内部上层的氯苯相留置在釜体主体1的内部,随后加入氢氧化钠溶液,再次进行1小时的搅拌以及1小时的静置操作,对于混合液分层所致的下层碱水直接通过防旋下料机构4排出,即可得到处理后的氯苯粗品溶液。Working principle: In the present invention, firstly, the waste liquid at the bottom of the chlorobenzene tower is introduced into the interior of the kettle body body 1 from the main feeding pipe 205 through external pumping, and then the driving motor 202 is turned on so that the output shaft of the driving motor 202 can drive the transmission shaft 5 to rotate, so that the transmission shaft 5 drives the sleeve column 62, the cleaning plate 74 and the scraping push plate 84 to rotate synchronously and in the same direction, and the heating steam is introduced into the interior of the kettle body body 1 through the first feed pipe 203, so that The temperature inside the kettle body 1 can reach 60-90°C, so that the inside of the kettle body 1 can be stirred and steam-heated, and then sulfuric acid is added dropwise to the inside of the kettle body 1 through the second feeding pipe 204, Ensure that the interior of the main body 1 of the kettle body does not boil violently, and the time for adding sulfuric acid must be controlled within 2-3 hours, and then turn off the input of heating steam, so that the internal temperature of the main body 1 of the kettle body is controlled at 40°C, and then through the first The second feed pipe 204 adds pure water to the interior of the kettle body body 1 for washing operation, and simultaneously starts stirring. The stirring time is controlled at 1 hour. After the stirring is completed, the liquid inside the
实施例3Example 3
参照图2,一种佳乐麝香氯苯后段废液的工业除杂方法,包括以下步骤:With reference to Fig. 2, the industrial impurity removal method of a kind of Jiale musk chlorobenzene rear section waste liquid, comprises the following steps:
S1:通过主投料管205向釜体主体1中加入3000kg氯苯塔底废液(氯苯80%、氯丙醇10%,甲缩醛和氯丙醇聚合物8%,茚满2%),开启驱动电机202,使得驱动电机202的输出轴能够间接带动套装柱62、清刷板74和刮料推动板84进行搅拌,将第一进料管203与外部的蒸汽供应管道连通,并且进行蒸汽输入加热,将釜内温度升到60-90℃;S1: Add 3000kg chlorobenzene tower bottom waste liquid (80% chlorobenzene, 10% chloropropanol, 8% methylal and chloropropanol polymer, 2% indane) to the
S2:将第二进料管204与外部管路连通,并且通过第二进料管204向釜体主体1的内部缓慢匀速滴加120-200kg浓度98%的硫酸,保证釜体主体1的内部不剧烈沸腾,需要在2-3小时内滴加结束;S2: Connect the
S3:关闭第一进料管203的蒸汽输入,使得釜体主体1的内部自然降温至40℃,通过第二进料管204向釜体主体1的内部加入纯水400kg进行水洗(将部分未参与反应的硫酸稀释),再进行搅拌1小时,而后静置1小时,混合液在釜体主体1的内部进行自然分层,将下层酸水通过防旋下料机构4排出至外部废水槽;S3: Close the steam input of the
S4:将釜体主体1内部上层得到的氯苯相留在釜体主体1的内部,并且通过第二进料管204加入5%的氢氧化钠溶液400kg(和硫酸进行中和反应,使反应液呈碱性),搅拌1小时,静置1小时自然分层,再通过防旋下料机构4放出下层碱水相,即可得到处理后的氯苯粗品溶液,经过气相色谱检测氯丙醇杂质峰≤1%,氯苯含量≥90%。S4: Leave the chlorobenzene phase obtained in the upper layer of the
实施例4Example 4
本实施例与实施例3的区别在于,S1阶段温度控制为60℃,在S2阶段滴加浓度98%的硫酸200kg,致使S3阶段下层酸水的排出量约420kg,以至于S4阶段下层碱水量约400kg,氯苯粗品产量约2700kg,经过气相色谱检测氯丙醇杂质峰0.6%,氯苯含量93%。The difference between this example and Example 3 is that the temperature in the S1 stage is controlled at 60°C, and 200 kg of sulfuric acid with a concentration of 98% is added dropwise in the S2 stage, so that the discharge of the lower layer of acid water in the S3 stage is about 420 kg, so that the amount of alkaline water in the lower layer of the S4 stage About 400kg, the output of crude chlorobenzene is about 2700kg, the impurity peak of chloropropanol is 0.6% and the content of chlorobenzene is 93% as detected by gas chromatography.
其他未描述步骤参照实施例3。Refer to Example 3 for other undescribed steps.
实施例5Example 5
本实施例与实施例3的区别在于,S1阶段温度控制为60℃,在S2阶段滴加浓度98%的硫酸180kg,致使S3阶段下层酸水的排出量约410kg,以至于S4阶段下层碱水量约400kg,氯苯粗品产量约2700kg,经过气相色谱检测氯丙醇杂质峰0.8%,氯苯含量92%。The difference between this example and Example 3 is that the temperature in the S1 stage is controlled at 60°C, and 180 kg of sulfuric acid with a concentration of 98% is added dropwise in the S2 stage, so that the discharge of the lower layer of acid water in the S3 stage is about 410 kg, so that the amount of alkaline water in the lower layer of the S4 stage About 400kg, the output of crude chlorobenzene is about 2700kg, the impurity peak of chloropropanol is 0.8% and the content of chlorobenzene is 92% through gas chromatography.
其他未描述步骤参照实施例3。Refer to Example 3 for other undescribed steps.
实施例6Example 6
本实施例与实施例3的区别在于,S1阶段温度控制为60℃,在S1阶段泵入釜体主体1内部的氯苯塔底废液含量为(氯苯84%,氯丙醇8%),S2阶段滴加浓度98%的硫酸150kg,致使S3阶段下层酸水的排出量约400kg,以至于S4阶段下层碱水量约400kg,氯苯粗品产量约2700kg,经过气相色谱检测氯丙醇杂质峰1%,氯苯含量90%。The difference between this example and Example 3 is that the temperature in the S1 stage is controlled at 60°C, and the content of the waste liquid at the bottom of the chlorobenzene column pumped into the
其他未描述步骤参照实施例3。Refer to Example 3 for other undescribed steps.
从实施例4-6可知,通过浓硫酸反应,氯苯塔底废液中氯丙醇杂质很明显消除,氯苯含量大幅度上升,可以作为粗品去精馏。Known from embodiment 4-6, by concentrated sulfuric acid reaction, chloropropanol impurity obviously eliminates in the waste liquid of chlorobenzene tower bottom, and chlorobenzene content rises substantially, can be used as crude product to rectify.
在本发明的描述中,需要理解的是,术语“中心”、“纵向”、“横向”、“长度”、“宽度”、“厚度”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”、“顺时针”、“逆时针”、“轴向”、“径向”、“周向”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。In describing the present invention, it should be understood that the terms "center", "longitudinal", "transverse", "length", "width", "thickness", "upper", "lower", "front", " Back", "Left", "Right", "Vertical", "Horizontal", "Top", "Bottom", "Inner", "Outer", "Clockwise", "Counterclockwise", "Axial" , "radial", "circumferential" and other indicated orientations or positional relationships are based on the orientations or positional relationships shown in the drawings, which are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying the referred device or Elements must have certain orientations, be constructed and operate in certain orientations, and therefore should not be construed as limitations on the invention.
在本发明中,除非另有明确的规定和限定,术语“设置”、“安装”、“相连”、“连接”、“固定”等术语应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或成一体;可以是机械连接,可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通或两个元件的相互作用关系。对于本领域的普通技术人员而言,可以根据具体情况理解上述术语在本发明中的具体含义。In the present invention, terms such as "installation", "installation", "connection", "connection" and "fixation" should be interpreted in a broad sense, for example, it may be a fixed connection or It is a detachable connection, or integrated; it can be a mechanical connection, a direct connection, or an indirect connection through an intermediary, and it can be the internal communication of two components or the interaction relationship between two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in the present invention according to specific situations.
本发明的控制方式是通过控制器来自动控制,控制器的控制电路通过本领域的技术人员简单编程即可实现,电源的提供也属于本领域的公知常识,并且本发明主要用来保护机械装置,所以本发明不再详细解释控制方式和电路连接。The control mode of the present invention is automatically controlled by a controller, and the control circuit of the controller can be realized through simple programming by those skilled in the art. The supply of power also belongs to common knowledge in this field, and the present invention is mainly used to protect mechanical devices , so the present invention will not explain the control method and circuit connection in detail.
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,根据本发明的技术方案及其发明构思加以等同替换或改变,都应涵盖在本发明的保护范围之内。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto, any person familiar with the technical field within the technical scope disclosed in the present invention, according to the technical solution of the present invention Any equivalent replacement or change of the inventive concepts thereof shall fall within the protection scope of the present invention.
Claims (11)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211197549.5A CN115626726B (en) | 2022-09-29 | 2022-09-29 | An industrial impurity removal system and method for the waste liquid of galaxol chlorobenzene rear stage |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211197549.5A CN115626726B (en) | 2022-09-29 | 2022-09-29 | An industrial impurity removal system and method for the waste liquid of galaxol chlorobenzene rear stage |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115626726A true CN115626726A (en) | 2023-01-20 |
CN115626726B CN115626726B (en) | 2025-04-01 |
Family
ID=84904311
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202211197549.5A Active CN115626726B (en) | 2022-09-29 | 2022-09-29 | An industrial impurity removal system and method for the waste liquid of galaxol chlorobenzene rear stage |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115626726B (en) |
Citations (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB772492A (en) * | 1953-04-10 | 1957-04-17 | Kerag Kesseischmiede App Und M | Improvements in methods of and apparatus for mixing gases with liquids |
BE873185A (en) * | 1978-01-02 | 1979-04-17 | Passavant Werke | METHOD AND DEVICE FOR DRAINING A GRAVITY SEPARATOR FOR LIGHT MATERIALS AND / OR SUSPENSION |
DE20121450U1 (en) * | 2001-10-16 | 2002-12-19 | Aco Severin Ahlmann Gmbh & Co. Kg, 24768 Rendsburg | Biological waste water treatment device |
US6949645B1 (en) * | 2004-05-20 | 2005-09-27 | Acura Pharmaceuticals, Inc. | Process for the production of opiates |
CN101987751A (en) * | 2009-08-04 | 2011-03-23 | 宁波市镇海捷登应用技术研究所 | Restaurant wastewater treatment device |
CN205999214U (en) * | 2016-08-31 | 2017-03-08 | 山东崇舜化工有限公司 | A kind of 3,3 ' dichloro-4,4s of production, 4 ' diaminodiphenyl-methane technique waste water processing meanss |
CN107778329A (en) * | 2017-10-22 | 2018-03-09 | 潍坊医学院 | A kind of preparation system of chlorophosphonitrile |
CN207204074U (en) * | 2017-07-26 | 2018-04-10 | 九江中星医药化工有限公司 | A kind of modified reactor |
CN107916899A (en) * | 2017-11-24 | 2018-04-17 | 西南石油大学 | A kind of vortex-induced vibration suppression device and method of the rotatable wavy orifice plate in change aperture |
CN108126642A (en) * | 2017-12-27 | 2018-06-08 | 安徽金善化工科技有限公司 | A kind of grignard reaction kettle prepared for triphenylphosphine |
CN208474203U (en) * | 2017-12-05 | 2019-02-05 | 浙江思科制冷股份有限公司 | A kind of anti-whirlpool cover of porous ductwork type |
CN208627297U (en) * | 2018-08-13 | 2019-03-22 | 江西华晨香料化工有限公司 | A kind of fragrance processing reaction kettle device |
CN110252268A (en) * | 2019-06-13 | 2019-09-20 | 江苏南大环保科技有限公司 | A kind of regeneration method of chlorobenzene production waste water absorption resin |
CN210459398U (en) * | 2019-07-31 | 2020-05-05 | 盐城丰华给水设备工程有限公司 | Stainless steel rotational flow preventer for water tank water suction pipeline |
CN211274633U (en) * | 2019-10-31 | 2020-08-18 | 济南美鲁威生物科技有限公司 | Reation kettle convenient to arrange material |
CN111718235A (en) * | 2020-07-21 | 2020-09-29 | 安徽金轩科技有限公司 | A kind of method for recovering Jiale Musk chlorobenzene solvent |
CN211800854U (en) * | 2020-04-03 | 2020-10-30 | 凯里市鑫明凯净水科技有限公司 | Reaction kettle for producing water treatment agent |
CN112221194A (en) * | 2020-10-23 | 2021-01-15 | 中国人民解放军61699部队 | Automatic settling kettle for extraction separation and control method |
CN214636333U (en) * | 2020-12-30 | 2021-11-09 | 洪湖源泰科技有限公司 | Polyaluminium chloride reaction kettle |
CN214714655U (en) * | 2020-12-24 | 2021-11-16 | 榆林市鑫盛源工矿科技有限公司 | Quick-cleaning filter device for antifreeze liquid processing |
CN215048849U (en) * | 2021-07-26 | 2021-12-07 | 青岛明朗环境工程有限公司 | A new type of shallow air flotation equipment |
CN114014741A (en) * | 2021-11-17 | 2022-02-08 | 安徽金轩科技有限公司 | A kind of industrial impurity removal method for recovering indane waste liquid from Jiale Musk |
CN114085124A (en) * | 2021-11-17 | 2022-02-25 | 安徽金轩科技有限公司 | Industrial impurity removal method for prophase waste liquid of Jiale musk chlorobenzene |
CN216573096U (en) * | 2021-12-27 | 2022-05-24 | 山东天洋新材料有限公司 | Reaction kettle for producing mine safe functional polymer material |
CN216605265U (en) * | 2021-12-22 | 2022-05-27 | 淄博盖米测控系统有限公司 | Pharmaceutical chemical industry reation kettle water oil layering detection device |
-
2022
- 2022-09-29 CN CN202211197549.5A patent/CN115626726B/en active Active
Patent Citations (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB772492A (en) * | 1953-04-10 | 1957-04-17 | Kerag Kesseischmiede App Und M | Improvements in methods of and apparatus for mixing gases with liquids |
BE873185A (en) * | 1978-01-02 | 1979-04-17 | Passavant Werke | METHOD AND DEVICE FOR DRAINING A GRAVITY SEPARATOR FOR LIGHT MATERIALS AND / OR SUSPENSION |
DE20121450U1 (en) * | 2001-10-16 | 2002-12-19 | Aco Severin Ahlmann Gmbh & Co. Kg, 24768 Rendsburg | Biological waste water treatment device |
US6949645B1 (en) * | 2004-05-20 | 2005-09-27 | Acura Pharmaceuticals, Inc. | Process for the production of opiates |
CN101987751A (en) * | 2009-08-04 | 2011-03-23 | 宁波市镇海捷登应用技术研究所 | Restaurant wastewater treatment device |
CN205999214U (en) * | 2016-08-31 | 2017-03-08 | 山东崇舜化工有限公司 | A kind of 3,3 ' dichloro-4,4s of production, 4 ' diaminodiphenyl-methane technique waste water processing meanss |
CN207204074U (en) * | 2017-07-26 | 2018-04-10 | 九江中星医药化工有限公司 | A kind of modified reactor |
CN107778329A (en) * | 2017-10-22 | 2018-03-09 | 潍坊医学院 | A kind of preparation system of chlorophosphonitrile |
CN107916899A (en) * | 2017-11-24 | 2018-04-17 | 西南石油大学 | A kind of vortex-induced vibration suppression device and method of the rotatable wavy orifice plate in change aperture |
CN208474203U (en) * | 2017-12-05 | 2019-02-05 | 浙江思科制冷股份有限公司 | A kind of anti-whirlpool cover of porous ductwork type |
CN108126642A (en) * | 2017-12-27 | 2018-06-08 | 安徽金善化工科技有限公司 | A kind of grignard reaction kettle prepared for triphenylphosphine |
CN208627297U (en) * | 2018-08-13 | 2019-03-22 | 江西华晨香料化工有限公司 | A kind of fragrance processing reaction kettle device |
CN110252268A (en) * | 2019-06-13 | 2019-09-20 | 江苏南大环保科技有限公司 | A kind of regeneration method of chlorobenzene production waste water absorption resin |
CN210459398U (en) * | 2019-07-31 | 2020-05-05 | 盐城丰华给水设备工程有限公司 | Stainless steel rotational flow preventer for water tank water suction pipeline |
CN211274633U (en) * | 2019-10-31 | 2020-08-18 | 济南美鲁威生物科技有限公司 | Reation kettle convenient to arrange material |
CN211800854U (en) * | 2020-04-03 | 2020-10-30 | 凯里市鑫明凯净水科技有限公司 | Reaction kettle for producing water treatment agent |
CN111718235A (en) * | 2020-07-21 | 2020-09-29 | 安徽金轩科技有限公司 | A kind of method for recovering Jiale Musk chlorobenzene solvent |
CN112221194A (en) * | 2020-10-23 | 2021-01-15 | 中国人民解放军61699部队 | Automatic settling kettle for extraction separation and control method |
CN214714655U (en) * | 2020-12-24 | 2021-11-16 | 榆林市鑫盛源工矿科技有限公司 | Quick-cleaning filter device for antifreeze liquid processing |
CN214636333U (en) * | 2020-12-30 | 2021-11-09 | 洪湖源泰科技有限公司 | Polyaluminium chloride reaction kettle |
CN215048849U (en) * | 2021-07-26 | 2021-12-07 | 青岛明朗环境工程有限公司 | A new type of shallow air flotation equipment |
CN114014741A (en) * | 2021-11-17 | 2022-02-08 | 安徽金轩科技有限公司 | A kind of industrial impurity removal method for recovering indane waste liquid from Jiale Musk |
CN114085124A (en) * | 2021-11-17 | 2022-02-25 | 安徽金轩科技有限公司 | Industrial impurity removal method for prophase waste liquid of Jiale musk chlorobenzene |
CN216605265U (en) * | 2021-12-22 | 2022-05-27 | 淄博盖米测控系统有限公司 | Pharmaceutical chemical industry reation kettle water oil layering detection device |
CN216573096U (en) * | 2021-12-27 | 2022-05-24 | 山东天洋新材料有限公司 | Reaction kettle for producing mine safe functional polymer material |
Also Published As
Publication number | Publication date |
---|---|
CN115626726B (en) | 2025-04-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109763137A (en) | A kind of device for production water supply javelle water | |
CN220091048U (en) | Chemical industry reation kettle mixes device in advance | |
CN211246554U (en) | Novel filler of nanometer is supplementary for modified production device | |
CN115626726A (en) | Industrial impurity removal system and method for jiale musk chlorobenzene rear-stage waste liquid | |
CN110605088A (en) | Production reaction kettle capable of improving uniformity of intermediate | |
CN113856230A (en) | Distillation still is used in essence spices production convenient to clearance | |
CN214717527U (en) | Horizontal centrifugal dehydration device | |
CN211451665U (en) | Hydrochloric acid levo-bubby-cause crystallization drying device | |
CN210022147U (en) | Reaction kettle device for producing petroleum drilling petroleum auxiliary agent | |
CN205496123U (en) | Slide glass belt cleaning device for experiments | |
CN219051330U (en) | Improved curing and stirring reaction kettle | |
CN208032418U (en) | A kind of chemical blender with long service life | |
CN215692325U (en) | Filter equipment is used in production and processing of ox gall salt | |
CN212720599U (en) | Bipyramid rotary dryer is used in terramycin production | |
CN212576135U (en) | Agitating unit is used in production of environment-friendly cutting fluid | |
CN210314085U (en) | Cassava is reaction unit for modified starch | |
CN215466573U (en) | Enzyme preparation draws uses raw materials belt cleaning device | |
CN208711055U (en) | A kind of crystal concentration precipitation device based on mvr technology | |
CN220507539U (en) | Drying device is used in production of nanometer silica | |
CN218740247U (en) | Centrifugal spray drier | |
CN219897823U (en) | Brightening agent purification is with compound cauldron | |
CN220071605U (en) | Graphite reation kettle convenient to wash | |
CN213915087U (en) | Efficient industrial chemicals rinsing device for chemical production | |
CN211026304U (en) | Multifunctional reaction kettle | |
CN109317444A (en) | A kind of water-saving raw material rinsing device of Chemical Manufacture |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |