TWI668328B - Method for zero-discharge phosphatization and saponification based on high-pressure closed circulation system - Google Patents

Method for zero-discharge phosphatization and saponification based on high-pressure closed circulation system Download PDF

Info

Publication number
TWI668328B
TWI668328B TW107129772A TW107129772A TWI668328B TW I668328 B TWI668328 B TW I668328B TW 107129772 A TW107129772 A TW 107129772A TW 107129772 A TW107129772 A TW 107129772A TW I668328 B TWI668328 B TW I668328B
Authority
TW
Taiwan
Prior art keywords
autoclave
phosphating
pressure
workpiece
kettle
Prior art date
Application number
TW107129772A
Other languages
Chinese (zh)
Other versions
TW202006185A (en
Inventor
楊景峰
鬱偉榮
沈鵬
汪海斌
Original Assignee
楊景峰
鬱偉榮
沈鵬
汪海斌
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 楊景峰, 鬱偉榮, 沈鵬, 汪海斌 filed Critical 楊景峰
Application granted granted Critical
Publication of TWI668328B publication Critical patent/TWI668328B/en
Publication of TW202006185A publication Critical patent/TW202006185A/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/82After-treatment
    • C23C22/83Chemical after-treatment
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/73Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals characterised by the process
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G5/00Cleaning or de-greasing metallic material by other methods; Apparatus for cleaning or de-greasing metallic material with organic solvents

Landscapes

  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)

Abstract

本發明公開了一種基於高壓密閉循環系統的零排放磷化、皂化的方法,包括高壓釜、分離釜、緩衝釜和液壓泵;採用如下步驟:步驟一、將工件裝入高壓釜中,然後進行密封使高壓釜耐壓範圍在20MPa以上;步驟二、CO 2除油除鏽;步驟三、循環分離;步驟四、高壓磷化;步驟五、循環分離二;步驟六、高壓皂化;步驟七、循環分離三; 步驟八、打開高壓釜,通風乾燥。採用本發明的技術方案能夠大大降低酸、鹼、工業水用量,勞動條件好,生產殘渣方便收集處理,不產生污水,不造成環境污染問題,實現了零排放。 The invention discloses a zero-emission phosphating and saponification method based on a high-pressure closed-cycle system, which includes an autoclave, a separation kettle, a buffer kettle, and a hydraulic pump. The following steps are adopted: Step 1. Load a workpiece into an autoclave, and then perform Sealing makes the autoclave pressure resistance range above 20MPa; step two, CO 2 degreasing and rust removal; step three, circulating separation; step four, high pressure phosphating; step five, circulating separation two; step six, high pressure saponification; step seven, Separate three cycles; Step eight, open the autoclave, ventilate and dry. Adopting the technical scheme of the invention can greatly reduce the consumption of acid, alkali and industrial water, good labor conditions, convenient collection and treatment of production residues, no sewage, no environmental pollution problems, and zero emissions.

Description

基於高壓密閉循環系統的零排放磷化、皂化的方法Zero-emission phosphating and saponification method based on high-pressure closed cycle system

本發明涉及金屬冷加工行業中的磷化、皂化前處理領域,尤其涉及一種基於高壓密閉循環系統的零排放磷化、皂化的方法。The invention relates to the field of phosphating and saponification pretreatment in the metal cold processing industry, and particularly relates to a zero-emission phosphating and saponification method based on a high-pressure closed cycle system.

金屬冷加工行業中,在進行拉絲、擠壓、深拉延等工序時,首先要在工件表面進行磷化-皂化處理,經過處理之後,能夠降低工件與模具之間的摩擦起到很好的潤滑效果。In the metal cold working industry, in the processes of wire drawing, extrusion, deep drawing, etc., the surface of the workpiece must first be phosphatized-saponified. After the treatment, it can reduce the friction between the workpiece and the mold and provide good lubrication. effect.

具體磷化處理的製作流程為:首先通過酸鹼對金屬工件的表面進行除油除鏽處理,處理之後的金屬工件採用水對其表面進行清洗;其次進行鋅系磷化處理,處理之後的金屬工件採用水對其表面進行清洗,再次採用硬脂酸鈉對金屬工件的表面進行皂化處理,處理完成之後進行乾燥處理。採用鋅系磷化的原因是,一、鋅系磷化膜皂化後形成潤滑性很好的硬脂酸鋅層,二、鋅系磷化操作溫度比較低,可在40、60或90℃條件下進行磷化處理。The specific production process of phosphating treatment is: first, the surface of the metal workpiece is degreased and derusted by acid and alkali, and the surface of the treated metal workpiece is washed with water; the second is the zinc-based phosphating treatment, and the treated metal The surface of the workpiece is washed with water, and the surface of the metal workpiece is saponified again with sodium stearate. After the processing is completed, the surface is dried. The reason for using zinc-based phosphating is that first, zinc-based phosphating film forms a zinc stearate layer with good lubricity after saponification. Second, zinc-based phosphating has a relatively low operating temperature, which can be at 40, 60 or 90 ° C. Phosphate treatment.

採用上述製作金屬工件進行除鏽時,會跟據不同金屬分別用鹽酸、硝酸、硫酸清洗除鏽,生成有毒害、嗆人的黃、紅煙霧,產生嚴重的腐蝕性三廢污染,並容易對清洗件的金屬本身:外層溶解形成過腐蝕,內部滲氫產生氫脆,危及使用安全、縮短使用壽命。另外整個過程需要多次進行水清洗,用水清洗稀釋廢工作液,會消耗、流失大量水資源,形成嚴重的污染和極大的浪費。When the above-mentioned production of metal workpieces is used for derusting, it will be washed and derusted with hydrochloric acid, nitric acid and sulfuric acid according to different metals, which will generate toxic, stinging yellow and red smoke, produce severe corrosive three waste pollution, and easy to clean. The metal itself: the outer layer dissolves to form over-corrosion, and the internal hydrogen permeation generates hydrogen embrittlement, which endangers the safety of use and shortens the service life. In addition, the entire process needs to be washed with water multiple times. Washing and diluting the waste working fluid with water will consume and lose a large amount of water resources, resulting in serious pollution and great waste.

有鑒於此,吾等發明人乃潛心進一步研究,並著手進行研發及改良,期以一較佳設作以解決上述問題,且在經過不斷試驗及修改後而有本發明之問世。In view of this, our inventors are concentrating on further research and proceeding with research and development and improvement, with a better design to solve the above problems, and the invention came out after continuous testing and modification.

為了解決現有技術存在的問題,本發明提供一種高壓密閉循環系統及採用該系統的零排放磷化、皂化的方法。In order to solve the problems existing in the prior art, the present invention provides a high-pressure closed cycle system and a zero-emission phosphating and saponifying method using the system.

為實現上述目的,本發明採用的技術方案是:一種基於高壓密閉循環系統的零排放磷化、皂化的方法,包括高壓釜、分離釜、緩衝釜、液壓泵和回收桶;採用步驟如下:To achieve the above objective, the technical solution adopted by the present invention is: a zero-emission phosphating and saponification method based on a high-pressure closed cycle system, including an autoclave, a separation kettle, a buffer kettle, a hydraulic pump, and a recovery barrel; the steps are as follows:

步驟一、將工件裝入高壓釜中,然後進行密封使高壓釜耐壓範圍在20MPa以上;Step 1: Put the workpiece into the autoclave, and then seal it so that the pressure range of the autoclave is above 20MPa;

步驟二、CO 2除油除鏽,二氧化碳經緩衝釜緩衝後通過液壓泵輸送給高壓釜,然後通過高壓釜內的文丘裡噴嘴向工件噴射高壓二氧化碳氣流對工件進行除鏽除油處理; Step 2: CO 2 degreasing and rust removal, carbon dioxide is buffered by a buffer tank, and then sent to the autoclave by a hydraulic pump, and then a high-pressure carbon dioxide gas stream is sprayed onto the workpiece through a venturi nozzle in the autoclave to derust and degrease the workpiece;

步驟三、循環分離:借助於緩衝釜和液壓泵將超臨界CO 2輸送到高壓釜內進行循環清理,直到高壓釜內潔淨,油漬和固體殘渣被超臨界CO 2推送入分離釜; Step 3: Circulating separation: The supercritical CO 2 is transported into the autoclave by means of a buffer tank and a hydraulic pump for cyclic cleaning until the autoclave is clean, and oil and solid residues are pushed into the separating tank by supercritical CO 2 ;

步驟四、高壓磷化:將磷化液通過液壓泵加壓注入高壓釜中,在高壓釜的攪拌器的作用下與釜內的高壓流體進行混合、稀釋;將高壓釜升溫到反應溫度,對工件表面進行磷化處理;磷化液在工件表面發生化學反應,形成磷化膜;反應結束後,將高壓釜中的流體導出到分離釜,分離收集磷化後的殘留物;Step 4. High-pressure phosphatization: Inject the phosphating solution into the autoclave under pressure by a hydraulic pump, mix and dilute it with the high-pressure fluid in the autoclave under the action of the agitator of the autoclave, and raise the autoclave to the reaction temperature. The surface of the workpiece is subjected to phosphating treatment; the phosphating solution chemically reacts on the surface of the workpiece to form a phosphating film; after the reaction is completed, the fluid in the autoclave is led to a separation kettle to separate and collect the phosphating residue;

步驟五、循環分離二:借助於緩衝釜和液壓泵將超臨界CO 2輸送到高壓釜內進行循環清理,直到高壓釜內潔淨; Step 5: Circulating separation 2: The supercritical CO 2 is transported into the autoclave by means of a buffer kettle and a hydraulic pump for circulating cleaning until the inside of the autoclave is clean;

步驟六、高壓皂化:將皂化通過液壓泵加壓注入高壓釜中,在高壓釜的攪拌器的作用下與釜內的高壓流體進行混合、稀釋;將高壓釜升溫到反應溫度,對工件表面進行磷化處理;磷化液在工件表面發生化學反應,形成皂化膜;反應結束後,將高壓釜中的流體導出到分離釜,分離收集皂化後的殘留物;Step 6. High-pressure saponification: Inject the saponification into the autoclave by means of a hydraulic pump, mix and dilute it with the high-pressure fluid in the autoclave under the action of the agitator of the autoclave; warm the autoclave to the reaction temperature, and carry out the work surface Phosphating treatment; the chemical reaction of the phosphating solution on the surface of the workpiece to form a saponification film; after the reaction is completed, the fluid in the autoclave is led to a separation kettle to separate and collect the residue after saponification;

步驟七、循環分離三:借助於緩衝釜和液壓泵將超臨界CO 2輸送到高壓釜內進行循環清理,直到高壓釜內潔淨; Step 7. Circulation separation III: The supercritical CO 2 is transported into the autoclave by means of a buffer kettle and a hydraulic pump for circulation cleaning until the autoclave is clean;

步驟八、乾燥:打開高壓釜,通風乾燥。Step 8. Drying: Open the autoclave and ventilate and dry.

進一步的改進,步驟五和步驟七中從分離釜分離後的二氧化碳經製冷、加壓,再通入高壓釜進行循環清洗。In a further improvement, the carbon dioxide separated from the separation kettle in steps 5 and 7 is cooled and pressurized, and then passed into the autoclave for cycle cleaning.

與現有技術相比,本發明的有益效果是採用本發明的技術方案後,可以通過調節溫度和壓力的變化來改變油漬、磷酸、磷酸鹽、硬脂酸鈉的溶解度,達到循環分離與收集的目的,大大降低酸、鹼、工水用量,化學溶液在封閉的管路中流動,無揮發、泄露,不向環境排除污水、廢液,勞動條件好,生產殘渣方便收集處理,不造成環境污染。Compared with the prior art, the beneficial effect of the present invention is that after the technical solution of the present invention is adopted, the solubility of oil stains, phosphoric acid, phosphates, and sodium stearate can be changed by adjusting changes in temperature and pressure to achieve circulation separation and collection. The purpose is to greatly reduce the amount of acid, alkali and working water. The chemical solution flows in the closed pipeline without volatilization and leakage. It does not exclude sewage and waste liquid from the environment. The working conditions are good. The production residues are easy to collect and treat without causing environmental pollution. .

關於吾等發明人之技術手段,茲舉數種較佳實施例配合圖式於下文進行詳細說明,俾供 鈞上深入瞭解並認同本發明。Regarding the technical means of our inventors, several preferred embodiments are described in detail below in conjunction with the drawings, for the purpose of understanding and agreeing with the present invention.

下面結合附圖對本發明優選的方案做進一步的闡述:The preferred solutions of the present invention will be further described below with reference to the drawings:

如第1圖和第2圖所示,一種基於高壓密閉循環系統的零排放磷化、皂化的方法,包括高壓釜、分離釜、緩衝釜、液壓泵和回收桶;採用步驟如下:As shown in Figures 1 and 2, a zero-emission phosphating and saponification method based on a high-pressure closed cycle system includes an autoclave, a separation kettle, a buffer kettle, a hydraulic pump, and a recovery barrel; the steps are as follows:

步驟一、將工件裝入高壓釜中,然後進行密封使高壓釜耐壓範圍在20MPa以上;Step 1: Put the workpiece into the autoclave, and then seal it so that the pressure range of the autoclave is above 20MPa;

步驟二、CO 2除油除鏽,二氧化碳經緩衝釜緩衝後通過液壓泵輸送給高壓釜,然後通過高壓釜內的文丘裡噴嘴向工件噴射高壓二氧化碳氣流對工件進行除鏽除油處理;在該步驟中,主要利用產生的二氧化碳“雪”(含有乾冰小顆粒)的動能動量除鏽,利用二氧化碳“雪”的化學溶解作用除油;然後通入超臨界二氧化碳流體,利用超臨界流體的溶解作用和沖刷作用將容器內的油污、固體顆粒物導出到分離釜,分離收集; Step 2: CO 2 degreasing and rust removal, carbon dioxide is buffered by a buffer tank and then sent to the autoclave by a hydraulic pump, and then a high-pressure carbon dioxide gas stream is sprayed onto the workpiece through a venturi nozzle in the autoclave to perform derusting and degreasing on the workpiece; In the step, the kinetic energy and momentum of the generated carbon dioxide “snow” (containing small particles of dry ice) are mainly used to remove rust, and the chemical dissolution of the carbon dioxide “snow” is used to remove oil; then the supercritical carbon dioxide fluid is passed in and the dissolution of the supercritical fluid is used The oil and solid particles in the container are exported to the separation kettle by the washing effect and separated and collected;

步驟三、循環分離:借助於緩衝釜和液壓泵將超臨界CO 2輸送到高壓釜內進行循環清理,直到高壓釜內潔淨,油漬和固體殘渣被超臨界CO 2推送入分離釜; Step 3: Circulating separation: The supercritical CO 2 is transported into the autoclave by means of a buffer tank and a hydraulic pump for cyclic cleaning until the autoclave is clean, and oil and solid residues are pushed into the separating tank by supercritical CO 2 ;

步驟四、高壓磷化:將磷化液通過液壓泵加壓注入高壓釜中,在高壓釜的攪拌器的作用下與釜內的高壓流體進行混合、稀釋;將高壓釜升溫到反應溫度,對工件表面進行磷化處理;磷化液在工件表面發生化學反應,形成磷化膜;反應結束後,將高壓釜中的流體導出到分離釜,分離收集磷化後的殘留物;Step 4. High-pressure phosphatization: Inject the phosphating solution into the autoclave under pressure by a hydraulic pump, mix and dilute it with the high-pressure fluid in the autoclave under the action of the agitator of the autoclave, and raise the autoclave to the reaction temperature. The surface of the workpiece is subjected to phosphating treatment; the phosphating solution chemically reacts on the surface of the workpiece to form a phosphating film; after the reaction is completed, the fluid in the autoclave is led to a separation kettle to separate and collect the phosphating residue;

步驟五、循環分離二:借助於緩衝釜和液壓泵將超臨界CO 2輸送到高壓釜內進行循環清理,直到高壓釜內潔淨;分離釜分離後的二氧化碳經製冷、加壓,再通入高壓釜進行循環清洗。 Step 5: Circulation separation 2: The supercritical CO 2 is transported into the autoclave by means of a buffer tank and a hydraulic pump to be circulated and cleaned until the autoclave is clean; the carbon dioxide separated by the separation tank is cooled, pressurized, and then passed into the high pressure The kettle was circulated for cleaning.

步驟六、高壓皂化:將皂化通過液壓泵加壓注入高壓釜中,在高壓釜的攪拌器的作用下與釜內的高壓流體進行混合、稀釋;將高壓釜升溫到反應溫度,對工件表面進行磷化處理;磷化液在工件表面發生化學反應,形成皂化膜;反應結束後,將高壓釜中的流體導出到分離釜,分離收集皂化後的殘留物;Step 6. High-pressure saponification: Inject the saponification into the autoclave by means of a hydraulic pump, mix and dilute it with the high-pressure fluid in the autoclave under the action of the agitator of the autoclave; warm the autoclave to the reaction temperature, and carry out the work surface Phosphating treatment; the chemical reaction of the phosphating solution on the surface of the workpiece to form a saponification film; after the reaction is completed, the fluid in the autoclave is led to a separation kettle to separate and collect the residue after saponification;

步驟七、循環分離三:借助於緩衝釜和液壓泵將超臨界CO 2輸送到高壓釜內進行循環清理,直到高壓釜內潔淨;分離釜分離後的二氧化碳經製冷、加壓,再通入高壓釜進行循環清洗。 Step Seven: Circulation separation III: The supercritical CO 2 is transported into the autoclave by means of a buffer tank and a hydraulic pump for circulation cleaning until the autoclave is clean; the carbon dioxide separated by the separation tank is cooled, pressurized, and then passed into the high pressure The kettle was circulated for cleaning.

步驟八、乾燥:打開高壓釜,通風乾燥。Step 8. Drying: Open the autoclave and ventilate and dry.

綜上所述,本發明所揭露之技術手段確能有效解決習知等問題,並達致預期之目的與功效,且申請前未見諸於刊物、未曾公開使用且具長遠進步性,誠屬專利法所稱之發明無誤,爰依法提出申請,懇祈 鈞上惠予詳審並賜准發明專利,至感德馨。In summary, the technical means disclosed in the present invention can effectively solve problems such as knowledge, and achieve the intended purpose and effect. It has not been published in publications before application, has not been publicly used, and has long-term progress. The invention referred to in the Patent Law is correct, and he filed an application in accordance with the law. He earnestly hopes that Jun will give him a detailed review and grant a patent for the invention.

惟以上所述者,僅為本發明之數種較佳實施例,當不能以此限定本發明實施之範圍,即大凡依本發明申請專利範圍及發明說明書內容所作之等效變化與修飾,皆應仍屬本發明專利涵蓋之範圍內。However, the above are only a few preferred embodiments of the present invention. When the scope of implementation of the present invention cannot be limited in this way, that is, equivalent changes and modifications made according to the scope of the patent application and the content of the invention specification of the present invention are all It should still fall within the scope of the invention patent.

〔本發明〕〔this invention〕

no

第1圖係基於高壓密閉循環系統的零排放磷化、皂化的方法的步驟原理框圖。 第2圖係基於高壓密閉循環系統的零排放磷化、皂化的方法的系統原理框圖。Figure 1 is a schematic block diagram of the steps of a zero-emission phosphating and saponifying method based on a high-pressure closed cycle system. Figure 2 is a system block diagram of a zero-emission phosphating and saponifying method based on a high-pressure closed-cycle system.

Claims (2)

一種基於高壓密閉循環系統的零排放磷化、皂化的方法,包括高壓釜、分離釜、緩衝釜、液壓泵和回收桶;其特徵在於:包括如下步驟: 步驟一、將工件裝入高壓釜中,然後進行密封使高壓釜耐壓範圍在20MPa以上; 步驟二、CO 2除油除鏽,二氧化碳經緩衝釜緩衝後通過液壓泵輸送給高壓釜,然後通過高壓釜內的文丘裡噴嘴向工件噴射高壓二氧化碳氣流對工件進行除鏽除油處理; 步驟三、循環分離:借助於緩衝釜和液壓泵將超臨界CO 2輸送到高壓釜內進行循環清理,直到高壓釜內潔淨,油漬和固體殘渣被超臨界CO 2推送入分離釜; 步驟四、高壓磷化:將磷化液通過液壓泵加壓注入高壓釜中,在高壓釜的攪拌器的作用下與釜內的高壓流體進行混合、稀釋;將高壓釜升溫到反應溫度,對工件表面進行磷化處理;磷化液在工件表面發生化學反應,形成磷化膜;反應結束後,將高壓釜中的流體導出到分離釜,分離收集磷化後的殘留物; 步驟五、循環分離二:借助於緩衝釜和液壓泵將超臨界CO 2輸送到高壓釜內進行循環清理,直到高壓釜內潔淨; 步驟六、高壓皂化:將皂化通過液壓泵加壓注入高壓釜中,在高壓釜的攪拌器的作用下與釜內的高壓流體進行混合、稀釋;將高壓釜升溫到反應溫度,對工件表面進行磷化處理;磷化液在工件表面發生化學反應,形成皂化膜;反應結束後,將高壓釜中的流體導出到分離釜,分離收集皂化後的殘留物; 步驟七、循環分離三:借助於緩衝釜和液壓泵將超臨界CO 2輸送到高壓釜內進行循環清理,直到高壓釜內潔淨; 步驟八、乾燥:打開高壓釜,通風乾燥。 A method for zero-emission phosphating and saponification based on a high-pressure closed-cycle system includes an autoclave, a separation kettle, a buffer kettle, a hydraulic pump, and a recovery barrel. The method is characterized in that it includes the following steps: Step 1. Load a workpiece into an autoclave Then, it is sealed to make the pressure range of the autoclave above 20MPa; Step 2. CO 2 degreasing and rust removal, carbon dioxide is buffered by the buffer tank and then sent to the autoclave by the hydraulic pump, and then sprayed to the workpiece through the venturi nozzle in the autoclave. High-pressure carbon dioxide gas is used to remove the rust and oil from the workpiece. Step 3. Cycle separation: Supercritical CO 2 is transported into the autoclave by means of a buffer tank and a hydraulic pump, and the cycle is cleaned until the autoclave is clean, oil stains and solid residues are removed. Supercritical CO 2 is pushed into the separation kettle; Step 4. High-pressure phosphating: the phosphating solution is injected into the autoclave by a hydraulic pump under pressure, and mixed with the high-pressure fluid in the kettle under the action of the agitator of the autoclave, and diluted; The autoclave is heated to the reaction temperature to perform phosphating on the surface of the workpiece; the phosphating solution chemically reacts on the surface of the workpiece to form a phosphating film After completion of the reaction, the autoclave was exported to the fluid separation vessel, separating the residue collected after phosphating; Step five, two separate cycle: a buffer tank and a hydraulic pump by means of supercritical CO 2 delivery into the autoclave cycle Clean up until the autoclave is clean. Step 6. High pressure saponification: Saponification is injected into the autoclave by means of a hydraulic pump, and it is mixed and diluted with the high pressure fluid in the autoclave under the action of the agitator of the autoclave. At the reaction temperature, the surface of the workpiece is phosphated; the phosphating solution chemically reacts on the surface of the workpiece to form a saponified film; after the reaction is completed, the fluid in the autoclave is led to a separation kettle to separate and collect the saponified residue; steps VII. Cyclic separation III: The supercritical CO 2 is transported into the autoclave by means of a buffer kettle and a hydraulic pump for circulation cleaning until the autoclave is clean. Step 8: Drying: Open the autoclave, ventilate and dry. 如申請專利範圍第1項所述之基於高壓密閉循環系統的零排放磷化、皂化的方法,其中,步驟五和步驟七中從分離釜分離後的二氧化碳經製冷、加壓,再通入高壓釜進行循環清洗。The zero-emission phosphating and saponification method based on the high-pressure closed-cycle system according to item 1 of the scope of the patent application, wherein the carbon dioxide separated from the separation kettle in step 5 and step 7 is cooled, pressurized, and then passed into the high pressure The kettle was circulated for cleaning.
TW107129772A 2018-07-02 2018-08-27 Method for zero-discharge phosphatization and saponification based on high-pressure closed circulation system TWI668328B (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CN201810709238.XA CN108754479B (en) 2018-07-02 2018-07-02 Zero-emission phosphating and saponification method based on high-pressure closed circulation system
CN201810709238.X 2018-07-02
??201810709238.X 2018-07-02

Publications (2)

Publication Number Publication Date
TWI668328B true TWI668328B (en) 2019-08-11
TW202006185A TW202006185A (en) 2020-02-01

Family

ID=63975326

Family Applications (1)

Application Number Title Priority Date Filing Date
TW107129772A TWI668328B (en) 2018-07-02 2018-08-27 Method for zero-discharge phosphatization and saponification based on high-pressure closed circulation system

Country Status (3)

Country Link
EP (1) EP3591091B1 (en)
CN (1) CN108754479B (en)
TW (1) TWI668328B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111089454B (en) * 2019-12-27 2022-02-11 科源动力科技有限公司 Working medium pump drying method in ORC low-temperature waste heat power generation equipment
DE102022108314A1 (en) * 2022-04-06 2023-10-12 Ecoclean Gmbh Method for passivating a surface of a workpiece and device for passivating workpieces
CN118613338A (en) * 2022-05-10 2024-09-06 杰拉尔德·亨里齐 Device and method for checking orifice and cleaning orifice by carbon dioxide

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000014301A1 (en) * 1998-09-08 2000-03-16 Henkel Corporation Alkaline liquid composition and method for degreasing metals
TW438631B (en) * 1993-09-07 2001-06-07 Hughes Aircraft Co Low cost equipment for cleaning using liquefiable gases
CN105665469A (en) * 2016-03-30 2016-06-15 江门市蓬江区永华金属线材厂 Non-acid-pickling derusting and phosphorizing continuous drawing equipment and drawing production method thereof
CN105908208A (en) * 2016-03-28 2016-08-31 绵阳维克切削液有限责任公司 Cold-rolled silicon steel normal-temperature zero-release oil removal agent and preparation method thereof
CN106216955A (en) * 2016-08-18 2016-12-14 无锡苏嘉法斯特汽车零配件有限公司 special steel transmission shaft tube manufacturing process

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0780772A (en) * 1993-09-16 1995-03-28 Nippon Steel Corp Surface treatment method of steel and its device
CN1155736C (en) * 2000-08-02 2004-06-30 暨南大学 Phosphonating liquid for cold deformation of iron and steel and its phosphonation process
WO2002016673A1 (en) * 2000-08-24 2002-02-28 Hideo Yoshida Electrochemical treating method such as electroplating and electrochemical reaction device therefor
CN105299335A (en) * 2014-07-31 2016-02-03 上海天阳钢管有限公司 Manufacturing method of carbon steel stainless steel double-metal polymerization pipe
CN105603415A (en) * 2014-11-19 2016-05-25 重庆江东摩托车配件有限公司 Saponification process
CN105695980A (en) * 2014-11-28 2016-06-22 重庆基石机械有限公司 Steel wire surface treatment process
CN105018920B (en) * 2015-08-04 2018-03-09 常熟市金华机械股份有限公司 A kind of phospholeum metaplasia production. art

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW438631B (en) * 1993-09-07 2001-06-07 Hughes Aircraft Co Low cost equipment for cleaning using liquefiable gases
WO2000014301A1 (en) * 1998-09-08 2000-03-16 Henkel Corporation Alkaline liquid composition and method for degreasing metals
CN105908208A (en) * 2016-03-28 2016-08-31 绵阳维克切削液有限责任公司 Cold-rolled silicon steel normal-temperature zero-release oil removal agent and preparation method thereof
CN105665469A (en) * 2016-03-30 2016-06-15 江门市蓬江区永华金属线材厂 Non-acid-pickling derusting and phosphorizing continuous drawing equipment and drawing production method thereof
CN106216955A (en) * 2016-08-18 2016-12-14 无锡苏嘉法斯特汽车零配件有限公司 special steel transmission shaft tube manufacturing process

Also Published As

Publication number Publication date
CN108754479B (en) 2020-04-21
TW202006185A (en) 2020-02-01
EP3591091A1 (en) 2020-01-08
EP3591091B1 (en) 2021-07-21
CN108754479A (en) 2018-11-06

Similar Documents

Publication Publication Date Title
TWI668328B (en) Method for zero-discharge phosphatization and saponification based on high-pressure closed circulation system
CN109136930A (en) Treatment method before surface oxidation of aluminum alloy and alkaline etching solution adopted by treatment method
CN104674263A (en) Metal surface cleaning method
CN104226719A (en) Aluminum alloy extrusion die washing method and device
CN102465307A (en) Stainless steel pipeline acid pickling method
CN103757647A (en) Steel material acid-washing and phosphorization method
CN114032555A (en) Cleaning process for medium pipeline of continuous casting equipment
CN103422051A (en) Method of removing copper-nickel/aluminum-graphite composite seal coating material
CN101328587A (en) Hydraulic tubing three-in-one acid cleaning process
CN203253743U (en) Cold-rolling pipe outer surface oil contamination on-line clearing device
CN102615285A (en) Automotive powder metallurgic ABS (acrylonitrile-butadiene-styrene) gear ring treating method
CN104357862A (en) Metal surface cleaning method
CN108150288B (en) Method for removing carbon deposition from engine conduit
CN103266326A (en) Wire rope pickling method
CN104294266B (en) Environment-friendly highly efficient brass passivation process
CN106756940A (en) A kind of chemical treatment method for surfaces for low carbon steel plate before welding
CN101956189A (en) Method for treating inner surface of steel drum
CN1011911B (en) Corrosion-resistant method for the outer and inner walls of steel pipe bundle
CN213327846U (en) Rust removal device before metal workpiece surface modification
CN102978597A (en) Spraying type comprehensive phosphate treating agent for cold-rolled sheet workpiece spraying coating and preparation method of spraying type comprehensive phosphate treating agent
CN103977685A (en) Acid-regeneration acid tail gas purification system by using spray roasting method and tail gas purification process
CN105018943B (en) A kind of pickling additive and preparation method thereof
CN110857473B (en) Safe, environment-friendly and zero-emission metal continuous oil removing method and device
CN103774168B (en) Manufacture again special dirt detergent and preparation method thereof
CN108531839A (en) A kind of environment-friendly type hot-dip galvanizing technique

Legal Events

Date Code Title Description
MM4A Annulment or lapse of patent due to non-payment of fees