TWI739535B - High-pressure hydrolysis device and method - Google Patents

High-pressure hydrolysis device and method Download PDF

Info

Publication number
TWI739535B
TWI739535B TW109126060A TW109126060A TWI739535B TW I739535 B TWI739535 B TW I739535B TW 109126060 A TW109126060 A TW 109126060A TW 109126060 A TW109126060 A TW 109126060A TW I739535 B TWI739535 B TW I739535B
Authority
TW
Taiwan
Prior art keywords
pressure
hydrolysis
space
container
pipeline
Prior art date
Application number
TW109126060A
Other languages
Chinese (zh)
Other versions
TW202206165A (en
Inventor
鐘介宏
Original Assignee
鐘介宏
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 鐘介宏 filed Critical 鐘介宏
Priority to TW109126060A priority Critical patent/TWI739535B/en
Application granted granted Critical
Publication of TWI739535B publication Critical patent/TWI739535B/en
Publication of TW202206165A publication Critical patent/TW202206165A/en

Links

Images

Landscapes

  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The present invention relates to a high-pressure hydrolysis method, which includes: placing a sealed hydrolysis container in a pressure tank; and applying a pressure of a certain value to the sealed hydrolysis container via a high-pressure device during a hydrolysis process and controlling an operating temperature to increase the reaction rate of hydrolysis. The present invention also relates to a high-pressure hydrolysis device for implementing the aforesaid hydrolysis method.

Description

高壓水解設備及其方法 High-pressure hydrolysis equipment and method

本發明係關於一種高壓水解方法,特別是指在水解過程中施以特定的壓力值及工作溫度,藉此提高水解的反應速率,本發明也是一種為施予該方法所使用的高壓水解設備。 The present invention relates to a high-pressure hydrolysis method, in particular to impose a specific pressure value and working temperature during the hydrolysis process, thereby increasing the reaction rate of the hydrolysis. The present invention is also a high-pressure hydrolysis equipment used for applying the method.

水解是一種化工單元過程,主要是物質與水反應,水解過程中重視的水解時間及水解的品質,如先前技術中華民國利公告號I642467「提升高木質素纖維原料糖化效率之混合型溶劑分離方法」,提供一種低水足跡之木質纖維素溶劑前處理方法,係使用溶劑與水進行木質纖維素組成之解聚分離之低水足跡前處理方法,藉由添加少量無機酸,於適當之反應溫度、壓力下,將木質素予以溶解且將半纖維素予以水解,兩者皆溶於液相,留下纖維素固渣。該發明係利用溶劑與水相對揮發性之差異,特別是相對低溫條件下,以低溫抽氣乾燥之方式輔助進行纖維素固渣之溶劑去除與回收,據此可顯著降低製程之用水量以及後續廢水處理量,達成製程低水足跡之目的,同時亦可達成原有溶劑前處理法所欲達成之酵素水解效率目標。而含有木質素與半纖維素水解產物之溶液則可藉由蒸發或稀釋之方式將溶劑濃度降低以析出木質素固體,藉以達成木質纖維素之三個主要組成之有效分離,達成木質纖維素之多元與充分利用之目的。 Hydrolysis is a chemical unit process, which mainly involves the reaction of substances with water. The hydrolysis time and quality of the hydrolysis are important in the hydrolysis process, such as the prior art Republic of China Announcement No. I642467 "Mixed solvent separation method to improve the saccharification efficiency of high lignin fiber raw materials" , Provide a low water footprint lignocellulose solvent pretreatment method, which uses a solvent and water to depolymerize and separate the lignocellulose composition. Under pressure, the lignin is dissolved and the hemicellulose is hydrolyzed, both of which dissolve in the liquid phase, leaving a solid cellulose residue. The invention utilizes the difference between the relative volatility of the solvent and water, especially under relatively low temperature conditions, assists the removal and recovery of the solvent of the cellulose solid residue by low-temperature air extraction and drying, which can significantly reduce the water consumption of the process and the follow-up The amount of wastewater treated can achieve the goal of low water footprint in the process, and at the same time can also achieve the goal of enzyme hydrolysis efficiency that the original solvent pretreatment method intends to achieve. The solution containing lignin and hemicellulose hydrolysate can be evaporated or diluted to reduce the solvent concentration to precipitate lignin solids, thereby achieving effective separation of the three main components of lignocellulose, and achieving lignocellulose The purpose of diversification and full utilization.

一般的水解往往需要長時間的反應,為了能有效解決長時間反應的問題,將會是未來水解技術最需要被重視的問題。 General hydrolysis often requires long-term reaction. In order to effectively solve the problem of long-term reaction, it will be the most important issue for hydrolysis technology in the future.

爰此,本發明人為了解決水解需要長時間反應的問題,而提出一種高壓水解設備,包含:一水解物容器,具有一水解空間;一壓力槽,配合一蓋體,所述壓力槽與該蓋體形成可啟閉的一高壓空間,該高壓空間置入前述水解物容器;一高壓裝置,連通該高壓空間;一控溫管路,包覆在該壓力槽;藉由該高壓裝置與該控溫管路,使該水解物容器在特定的一壓力值及一工作溫度下完成水解 Therefore, in order to solve the problem that hydrolysis requires a long time to react, the inventor proposes a high-pressure hydrolysis equipment, which includes: a hydrolysate container with a hydrolysis space; a pressure tank fitted with a cover, the pressure tank and the The cover forms a high-pressure space that can be opened and closed, and the high-pressure space is placed in the aforementioned hydrolysate container; a high-pressure device is connected to the high-pressure space; a temperature control pipeline is wrapped around the pressure tank; The temperature control pipeline enables the hydrolysate container to complete the hydrolysis at a specific pressure value and a working temperature

其中,該水解物容器包含有一密封蓋、一容器及一止漏件,該容器的一開口處結合有該止漏件,且該密封蓋蓋合在該容器上,形成前述水解空間。又進一步說明,該高壓裝置包含有一高壓幫浦、一壓力控制器、一增壓閥門及一第一管線,所述第一管線依序連通該高壓幫浦、該壓力控制器及該增壓閥門,該增壓閥門朝向該高壓空間,並控制連通或關閉該高壓空間。 Wherein, the hydrolysate container includes a sealed lid, a container, and a leak-proof element. An opening of the container is combined with the leak-proof element, and the sealed cover is closed on the container to form the aforementioned hydrolysis space. It is further explained that the high-pressure device includes a high-pressure pump, a pressure controller, a pressure-increasing valve, and a first pipeline, and the first pipeline connects the high-pressure pump, the pressure controller, and the pressure-increasing valve in sequence , The pressure-increasing valve faces the high-pressure space, and controls to communicate or close the high-pressure space.

又進一步,包含有一洩壓管路,該洩壓管路具有一第二管線及一洩壓閥門,該洩壓閥門朝向該高壓空間,並控制連通或關閉該高壓空間,將該高壓流體導出至該高壓空間。 Still further, a pressure relief pipeline is included. The pressure relief pipeline has a second pipeline and a pressure relief valve. The pressure relief valve faces the high-pressure space and controls to communicate with or close the high-pressure space to export the high-pressure fluid to The high-pressure space.

特別說明到,該高壓幫浦係導入一高壓流體至該高壓空間,所述高壓流體自該高壓空間朝向該水解物容器之該密封蓋施予壓力,使該密封蓋壓縮該水解空間,藉此提供前述壓力值。 Specifically, the high-pressure pump introduces a high-pressure fluid into the high-pressure space, and the high-pressure fluid applies pressure from the high-pressure space toward the sealing cover of the hydrolysate container, so that the sealing cover compresses the hydrolysis space, thereby Provide the aforementioned pressure value.

其中,該控溫管路包含有一螺旋管線,該螺旋管線具有一入口及一出口,該螺旋管線包覆在前述壓力槽,該螺旋管線注入有一控溫流體,用以提供前述熱能。 Wherein, the temperature control pipeline includes a spiral pipeline having an inlet and an outlet, the spiral pipeline is wrapped in the pressure groove, and the spiral pipeline is injected with a temperature control fluid to provide the aforementioned heat energy.

本發明也是一種高壓水解方法,包含:將一水解原料置入於密封的一水解物容器的一水解空間中;配置一高壓空間,將前述水解物容器置入該高壓空間;提供該高壓空間一熱能,控制該高壓空間的一工作溫度;藉由該高壓空間對該水解物容器的該水解空間施予70至250kg/cm2的一壓力,以及控制該工作溫度介於攝氏30至70℃,讓該水解原料在該壓力值及該工作溫度下完成水解。 The present invention is also a high-pressure hydrolysis method, including: placing a hydrolyzed raw material in a hydrolysis space of a sealed hydrolysate container; configuring a high-pressure space, and placing the aforementioned hydrolysate container in the high-pressure space; providing the high-pressure space; Thermal energy controls a working temperature of the high-pressure space; applies a pressure of 70 to 250 kg/cm 2 to the hydrolysis space of the hydrolysate container through the high-pressure space, and controls the working temperature to be between 30 and 70°C, Let the hydrolyzed raw material complete the hydrolysis at the pressure value and the working temperature.

進一步,所述高壓空間係透過一高壓流體施壓於該水解物容器。 Further, the high-pressure space is pressurized on the hydrolysate container through a high-pressure fluid.

進一步,所述高壓空間係透過一高壓裝置的一機械能施壓於該水解物容器。 Further, the high-pressure space is pressurized on the hydrolysate container through a mechanical energy of a high-pressure device.

進一步,包含有一洩壓管路,在水解完成後,排洩該高壓空間的該高壓流體。 Furthermore, a pressure relief pipeline is included to discharge the high-pressure fluid in the high-pressure space after the hydrolysis is completed.

進一步,可以在水解原料放入時添加所對應的酵素。 Furthermore, the corresponding enzyme can be added when the hydrolyzed raw material is put in.

根據上述技術特徵可達成以下功效: According to the above technical features, the following effects can be achieved:

1.將水解原料密封在水解物容器中,並施以一定的壓力值及工作溫度,讓整體的水解速度可以縮短至原先速率的1/5。 1. Seal the hydrolyzed raw materials in the hydrolysate container, and apply a certain pressure value and working temperature, so that the overall hydrolysis rate can be shortened to 1/5 of the original rate.

2.所添加的酵素,可以依據被水解物的性質去挑選,針對特定的化學鍵進行破壞,增加水解速率及品質。 2. The added enzymes can be selected according to the nature of the hydrolyzed product, and destroy specific chemical bonds to increase the rate and quality of the hydrolysis.

3.水解過程中所使用的螺旋管線加熱穩定,不會直接接觸導熱流體,有助於維持一定的溫度環境。 3. The spiral pipeline used in the hydrolysis process is stable in heating and will not directly contact the heat transfer fluid, which helps to maintain a certain temperature environment.

4.水解過程中壓縮該水解物容器的壓力源不限定是流體還是機械能,可以依照現場狀況去調整,自由度高。 4. During the hydrolysis process, the pressure source for compressing the hydrolysate container is not limited to fluid or mechanical energy, and can be adjusted according to site conditions, with a high degree of freedom.

1:水解物容器 1: Hydrolysate container

11:容器 11: container

12:開口處 12: Opening

13:水解空間 13: Hydrolysis space

14:止漏件 14: Stop leakage

15:密封蓋 15: Sealing cover

16:水解原料 16: Hydrolyzed raw materials

2:壓力槽 2: Pressure tank

21:蓋體 21: Lid

22:高壓空間 22: High-pressure space

3:高壓裝置 3: High pressure device

31:高壓幫浦 31: high pressure pump

32:壓力控制器 32: Pressure controller

33:增壓閥門 33: Booster valve

34:第一管線 34: The first pipeline

A:高壓流體 A: High pressure fluid

4:洩壓管路 4: Pressure relief pipeline

41:第二管線 41: second pipeline

42:洩壓閥門 42: Pressure relief valve

5:控溫管路 5: Temperature control pipeline

51:螺旋管線 51: spiral line

52:入口 52: entrance

53:出口 53: Exit

[第一圖]係本發明之高壓水解方法的實施例之流程方塊示意圖。 [The first figure] is a schematic block diagram of the flow of an embodiment of the high-pressure hydrolysis method of the present invention.

[第二圖]係本發明之高壓水解方法的實施例之實施示意圖(一)。 [The second figure] is a schematic diagram (1) of an embodiment of the high-pressure hydrolysis method of the present invention.

[第三圖]係本發明之高壓水解方法的實施例之實施示意圖(二)。 [Third Figure] is a schematic diagram (2) of an embodiment of the high-pressure hydrolysis method of the present invention.

[第四圖]係本發明之高壓水設備造示意圖(一)。 [Fourth Figure] is a schematic diagram of the high-pressure water equipment of the present invention (1).

[第五圖]係本發明之高壓水設備造示意圖(二)。 [Fifth Figure] is a schematic diagram of the high-pressure water equipment of the present invention (2).

[第六圖]係本發明之高壓水設備造示意圖(三)。 [Figure 6] is a schematic diagram of the construction of the high-pressure water equipment of the present invention (3).

綜合上述技術特徵,本發明高壓水解方法的主要功效將可於下述實施例清楚呈現。 Based on the above technical features, the main effects of the high-pressure hydrolysis method of the present invention will be clearly presented in the following examples.

請參考第一圖該實施例的高壓水解方法,包含以下步驟:首先,在本實施例中所採用的一水解原料係為一菇類(植物纖維),當然也可以換成其他被水解物,例如燕窩等,不依此為限。將該水解原料與水混合,同時選擇性地添加對應的一酵素,在本實施例中,所使用的該酵素為纖維分解酵素,濃度百分比為0.05至1%。使其反應更快速,並置入密封的一水解物容器的一水解空間中備用,該水解物容器雖然密封,但可以變化容積,藉此使水解空間接受外來的壓力。 Please refer to the first figure. The high-pressure hydrolysis method of this embodiment includes the following steps: First, the hydrolyzed raw material used in this embodiment is a mushroom (plant fiber). Of course, it can also be replaced with other hydrolyzed substances. For example, bird's nest, etc., are not limited to this. The hydrolyzed raw material is mixed with water, and a corresponding enzyme is selectively added at the same time. In this embodiment, the enzyme used is a cellulolytic enzyme, and the concentration percentage is 0.05 to 1%. The reaction is faster, and it is placed in a hydrolysis space of a sealed hydrolysate container for later use. Although the hydrolysate container is sealed, the volume can be changed, thereby allowing the hydrolysis space to receive external pressure.

配置一高壓空間,將前述水解物容器放入在該高壓空間中,所述高壓空間對該水解物容器的該水解空間施予一壓力,請參考第二圖至第三圖所示,圖中係呈現該高壓空間對該水解物容器施予該壓力,所述壓力可以是利用 一高壓流體來施壓於該水解物容器,前述水解物容器,並同時需要配置一洩壓管路,在水解完成後,排洩該高壓空間的該高壓流體。再更進一步說明,該高壓流體可以是液體或氣體,以液體的水來說明,於該高壓空間導入高壓的水,高壓的水施壓於該水解物容器的水解空間,使水解原料接受該壓力。又或者,該壓力也可以是機構所達成的機械能,透過機構來施壓於水解物容器的水解空間。 Configure a high-pressure space, put the aforementioned hydrolysate container into the high-pressure space, and the high-pressure space applies a pressure to the hydrolyzed space of the hydrolysate container. Please refer to the second to third figures. It shows that the high-pressure space exerts the pressure on the hydrolysate container, and the pressure can be used A high-pressure fluid is used to press the hydrolysate container, the aforementioned hydrolysate container, and a pressure relief pipeline needs to be configured at the same time. After the hydrolysis is completed, the high-pressure fluid in the high-pressure space is discharged. To further illustrate, the high-pressure fluid can be liquid or gas, and it is described as liquid water. High-pressure water is introduced into the high-pressure space, and the high-pressure water is pressed into the hydrolysis space of the hydrolysate container to make the hydrolyzed raw materials receive the pressure. . Or, the pressure can also be the mechanical energy achieved by the mechanism, and the pressure is applied to the hydrolysis space of the hydrolysate container through the mechanism.

本實施例同時配置一控溫管路,連通至前述高壓空間,用以提供該高壓空間一熱能,控制該高壓空間的一工作溫度。 In this embodiment, a temperature control pipeline is also configured to connect to the aforementioned high-pressure space to provide thermal energy in the high-pressure space and control a working temperature of the high-pressure space.

準備完成後,根據該菇類的特性,我們將該高壓空間中的一壓力值設定在70~250kg/cm2,以及設定該工作溫度在攝氏30~70℃之間,反應10~120分鐘直至完成水解,在過程中該高壓空間的該高壓流體施壓於該水解物容器,使該水解原料在特定的該壓力值及該工作溫度下快速地完成水解。 After the preparation is completed, according to the characteristics of the mushrooms, we set a pressure value in the high-pressure space at 70~250kg/cm 2 , and set the working temperature at 30~70℃, and react for 10~120 minutes until When the hydrolysis is completed, the high-pressure fluid in the high-pressure space is pressurized on the hydrolysate container during the process, so that the hydrolyzed raw material can quickly complete the hydrolysis at the specific pressure value and the working temperature.

本發明另外一實施例為一種高壓水解設備,請參考第四圖,該高壓水解設備包含: 一水解物容器1,在本實施例中,該水解物容器1為圓筒設計的一容器11,該容器11具有一開口處12,及連通該開口處12的一水解空間13,該容器11的該開口處12套覆有一止漏件14,再以一密封蓋15蓋合在該容器11上,形成前述水解空間13。從第四圖可以明顯看到,該密封蓋15略小於該容器11,使該密封蓋15能夠活動於該容器11中,並在該密封蓋15與該容器11接觸位置環設有一止漏件14,主要是避免水解過程中異物進入。 Another embodiment of the present invention is a high-pressure hydrolysis equipment. Please refer to Figure 4. The high-pressure hydrolysis equipment includes: A hydrolysate container 1. In this embodiment, the hydrolysate container 1 is a container 11 with a cylindrical design. The container 11 has an opening 12 and a hydrolysis space 13 communicating with the opening 12. The container 11 The opening 12 is covered with an anti-leak component 14, and then a sealing cap 15 is used to cover the container 11 to form the aforementioned hydrolysis space 13. It can be clearly seen from the fourth figure that the sealing cap 15 is slightly smaller than the container 11, so that the sealing cap 15 can move in the container 11, and a leak stop is provided around the contact position of the sealing cap 15 and the container 11 14. The main purpose is to avoid the entry of foreign matter during the hydrolysis process.

在本實施例中取一水解原料16置入在該水解空間空間13中,本實施例中該水解原料16所採用的是菇類,進一步,說明在該密封蓋15上更包含有一拉環151,主要是方便勾住此處拉起處理 In this embodiment, a hydrolyzed raw material 16 is taken and placed in the hydrolyzed space 13. In this embodiment, the hydrolyzed raw material 16 is mushrooms. Further, it is illustrated that the sealing cover 15 further includes a pull ring 151 , Mainly to facilitate the hook up here to handle

一壓力槽2,配合一蓋體21,所述蓋體21蓋合在該壓力槽2上,與該壓力槽2形成可開啟或關閉的一高壓空間22,並在所述高壓空間22中置入前述水解物容器1。 A pressure groove 2 is matched with a cover 21, the cover 21 is closed on the pressure groove 2, and the pressure groove 2 forms a high-pressure space 22 that can be opened or closed, and is placed in the high-pressure space 22 Into the aforementioned hydrolysate container 1.

請接續參考第五圖所示,在該壓力槽2任一側連通有一高壓裝置3,該高壓裝置3包含一高壓幫浦31、一壓力控制器32、一增壓閥門33及一第一管線34,如圖中可以清楚了解在該第一管線中填入有一高壓流體A,在本實施例中該高壓流體A係為水,並透過該壓力控制器32調整壓力,再以高壓幫浦31進行加壓動作,最後再將加壓完成的水,送到該增壓閥門33,該增壓閥門33朝向該高壓空間22,並控制連通或關閉該高壓空間22,藉以提供不同壓力的水來改變該高壓空間22的一壓力值。並在該壓力槽2任一側設有一洩壓管路4,連通該高壓空間22,該洩壓管路4包含有一第二管線41及一洩壓閥門42,該洩壓閥門42朝向該高壓空間,並控制連通或關閉該高壓空間22,當該洩壓閥門42開啟時,該高壓流體將由該第二管線41導出該高壓空間22。 Please continue to refer to the fifth figure. A high-pressure device 3 is connected to either side of the pressure tank 2. The high-pressure device 3 includes a high-pressure pump 31, a pressure controller 32, a pressure-increasing valve 33, and a first pipeline. 34. As shown in the figure, it can be clearly seen that a high-pressure fluid A is filled in the first pipeline. In this embodiment, the high-pressure fluid A is water, and the pressure is adjusted through the pressure controller 32, and then the high-pressure pump 31 is used. Perform pressurization, and finally send the pressurized water to the pressurization valve 33. The pressurization valve 33 faces the high-pressure space 22 and controls to communicate or close the high-pressure space 22 to provide water with different pressures. A pressure value of the high-pressure space 22 is changed. A pressure relief pipeline 4 is provided on either side of the pressure tank 2 to communicate with the high pressure space 22. The pressure relief pipeline 4 includes a second pipeline 41 and a pressure relief valve 42 facing the high pressure When the pressure relief valve 42 is opened, the high-pressure fluid will be led out of the high-pressure space 22 through the second pipeline 41.

請接續參閱第六圖所示,一控溫管路5,包含有一螺旋管線51,該螺旋管線51具有一入口52及一出口53,該螺旋管線51包覆貼緊在前述壓力槽2外側,該螺旋管線51注入有一控溫流體,在本實施例中該控溫流體可以是水,也可以是廢熱水,用以提供一熱能,並控制一工作溫度。 Please refer to Fig. 6 continuously. A temperature control pipeline 5 includes a spiral pipeline 51 having an inlet 52 and an outlet 53, and the spiral pipeline 51 is wrapped and tightly attached to the outside of the pressure tank 2. The spiral pipeline 51 is filled with a temperature control fluid. In this embodiment, the temperature control fluid can be water or waste hot water to provide thermal energy and control a working temperature.

請參考第六圖所示,藉由該高壓裝置3將加壓完成的水注入到該高壓空間22中,水不斷的壓到該密封蓋15,使其下降進而壓縮該水解原料16, 並透過該控溫管路5,使該水解物容器11中的該水解原料16在該壓力值及一工作溫度下完成水解。在本實施例,我們將該一壓力值設定在70~250kg/cm2,以及設定該工作溫度在攝氏30~70℃之間,反應10~120分鐘。 Please refer to the sixth figure. The pressurized water is injected into the high-pressure space 22 by the high-pressure device 3, and the water is continuously pressed to the sealing cover 15, causing it to drop and compress the hydrolyzed raw material 16, and pass through The temperature control pipeline 5 enables the hydrolyzed raw material 16 in the hydrolysate container 11 to complete the hydrolysis at the pressure value and a working temperature. In this embodiment, we set the pressure value at 70~250kg/cm 2 , and set the working temperature at 30~70°C, and react for 10~120 minutes.

綜合上述實施例之說明,當可充分瞭解本發明之操作、使用及本發明產生之功效,惟以上所述實施例僅係為本發明之較佳實施例,當不能以此限定本發明實施之範圍,即依本發明申請專利範圍及發明說明內容所作簡單的等效變化與修飾,皆屬本發明涵蓋之範圍內。 Based on the description of the above embodiments, when one can fully understand the operation and use of the present invention and the effects of the present invention, but the above embodiments are only the preferred embodiments of the present invention, and the implementation of the present invention cannot be limited by this. The scope, that is, simple equivalent changes and modifications made according to the scope of the patent application of the present invention and the content of the description of the invention, are all within the scope of the present invention.

Claims (10)

一種高壓水解設備,包含:一水解物容器,具有一水解空間;一壓力槽,配合一蓋體,所述壓力槽與該蓋體形成可啟閉的一高壓空間,該高壓空間置入前述水解物容器;一高壓裝置,連通該高壓空間;一控溫管路,包覆在該壓力槽;藉由該高壓裝置與該控溫管路,使該水解物容器在特定的一壓力值及一工作溫度下完成水解。 A high-pressure hydrolysis equipment includes: a hydrolysate container with a hydrolysis space; a pressure tank matched with a cover, the pressure tank and the cover form a high-pressure space that can be opened and closed, and the high-pressure space is placed in the hydrolysis space. Material container; a high-pressure device connected to the high-pressure space; a temperature-controlled pipeline wrapped in the pressure tank; by the high-pressure device and the temperature-controlled pipeline, the hydrolysate container is at a specific pressure value and a Hydrolysis is completed at working temperature. 如請求項1之高壓水解設備,其中該水解物容器包含有一密封蓋、一容器及一止漏件,該容器的一開口處結合有該止漏件,且該密封蓋蓋合在該容器上,形成前述水解空間。 The high-pressure hydrolysis equipment of claim 1, wherein the hydrolysate container includes a sealed lid, a container, and a leak-proof member, the leak-proof member is combined at an opening of the container, and the sealing cover is closed on the container , Form the aforementioned hydrolysis space. 如請求項1或2任一項所述之高壓水解設備,其中該高壓裝置包含有一高壓幫浦、一壓力控制器、一增壓閥門及一第一管線,所述第一管線依序連通該高壓幫浦、該壓力控制器及該增壓閥門,該增壓閥門朝向該高壓空間,並控制連通或關閉該高壓空間。 The high-pressure hydrolysis equipment according to any one of claim 1 or 2, wherein the high-pressure device includes a high-pressure pump, a pressure controller, a pressure-increasing valve, and a first pipeline, and the first pipeline is connected to the The high-pressure pump, the pressure controller and the pressure-increasing valve, the pressure-increasing valve faces the high-pressure space, and controls to communicate or close the high-pressure space. 如請求項3之高壓水解設備,進一步包含有一洩壓管路,該洩壓管路具有一第二管線及一洩壓閥門,該洩壓閥門朝向該高壓空間,並控制連通或關閉該高壓空間,將該高壓流體導出至該高壓空間。 For example, the high-pressure hydrolysis equipment of claim 3, further comprising a pressure relief pipeline, the pressure relief pipeline has a second pipeline and a pressure relief valve, the pressure relief valve faces the high pressure space and controls to communicate or close the high pressure space , Lead the high-pressure fluid to the high-pressure space. 如請求項3之高壓水解設備,其中該高壓幫浦係導入一高壓流體至該高壓空間,所述高壓流體自該高壓空間朝向該水解物容器之該密封蓋施予壓力,使該密封蓋壓縮該水解空間,藉此提供前述壓力值。 The high-pressure hydrolysis equipment of claim 3, wherein the high-pressure pump introduces a high-pressure fluid into the high-pressure space, and the high-pressure fluid applies pressure from the high-pressure space toward the sealing cover of the hydrolysate container to compress the sealing cover The hydrolysis space thereby provides the aforementioned pressure value. 如請求項1之高壓水解設備,其中該控溫管路包含有一螺旋管線,該螺旋管線具有一入口及一出口,該螺旋管線包覆在前述壓力槽,該螺旋管線注入有一控溫流體,用以提供前述熱能。 The high-pressure hydrolysis equipment of claim 1, wherein the temperature control pipeline includes a spiral pipeline, the spiral pipeline has an inlet and an outlet, the spiral pipeline is wrapped in the pressure tank, and the spiral pipeline is filled with a temperature control fluid. To provide the aforementioned thermal energy. 一種高壓水解方法,包含:將一水解原料置入密封的一水解物容器的一水解空間中;配置一高壓空間,將前述水解物容器置入該高壓空間;提供該高壓空間一熱能,控制該高壓空間的一工作溫度;藉由該高壓空間對該水解物容器的該水解空間施予70至250kg/cm2的一壓力,以及控制該工作溫度介於攝氏30至70℃,讓該水解原料在該壓力值及該工作溫度下完成水解。 A high-pressure hydrolysis method includes: placing a hydrolyzed raw material into a hydrolysis space of a sealed hydrolysate container; configuring a high-pressure space, and placing the aforementioned hydrolysate container into the high-pressure space; providing thermal energy in the high-pressure space to control the A working temperature of the high-pressure space; apply a pressure of 70 to 250 kg/cm 2 to the hydrolysis space of the hydrolysate container through the high-pressure space, and control the working temperature to be between 30 and 70°C to allow the hydrolyzed raw material The hydrolysis is completed at the pressure value and the working temperature. 如請求項7之高壓水解方法,所述高壓空間係透過一高壓流體施壓於該水解物容器。 According to the high-pressure hydrolysis method of claim 7, the high-pressure space is pressurized on the hydrolysate container through a high-pressure fluid. 如請求項7之高壓水解方法,所述高壓空間係透過一高壓裝置的一機械能施壓於該水解物容器。 According to the high-pressure hydrolysis method of claim 7, the high-pressure space is pressurized on the hydrolysate container through a mechanical energy of a high-pressure device. 如請求項8之高壓水解方法,進一步包含有一洩壓管路,在水解完成後,排洩該高壓空間的該高壓流體。 For example, the high-pressure hydrolysis method of claim 8, further comprising a pressure relief pipeline for draining the high-pressure fluid in the high-pressure space after the hydrolysis is completed.
TW109126060A 2020-07-31 2020-07-31 High-pressure hydrolysis device and method TWI739535B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW109126060A TWI739535B (en) 2020-07-31 2020-07-31 High-pressure hydrolysis device and method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW109126060A TWI739535B (en) 2020-07-31 2020-07-31 High-pressure hydrolysis device and method

Publications (2)

Publication Number Publication Date
TWI739535B true TWI739535B (en) 2021-09-11
TW202206165A TW202206165A (en) 2022-02-16

Family

ID=78778124

Family Applications (1)

Application Number Title Priority Date Filing Date
TW109126060A TWI739535B (en) 2020-07-31 2020-07-31 High-pressure hydrolysis device and method

Country Status (1)

Country Link
TW (1) TWI739535B (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006007157A (en) * 2004-06-29 2006-01-12 Japan Organo Co Ltd Reaction device and reaction method
CN102223948A (en) * 2008-09-25 2011-10-19 B.H.哈里森 Dual vessel reactor
CN206366378U (en) * 2016-12-01 2017-08-01 西安交通大学 The reactor and continous way system of hydro-thermal dewater treatment high-moisture percentage organic matter
TW202019673A (en) * 2018-11-20 2020-06-01 海崴生物科技股份有限公司 Continuous plant extraction machine capable of automatically and rapidly extracting plant samples to achieve better extraction rate

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006007157A (en) * 2004-06-29 2006-01-12 Japan Organo Co Ltd Reaction device and reaction method
CN102223948A (en) * 2008-09-25 2011-10-19 B.H.哈里森 Dual vessel reactor
CN206366378U (en) * 2016-12-01 2017-08-01 西安交通大学 The reactor and continous way system of hydro-thermal dewater treatment high-moisture percentage organic matter
TW202019673A (en) * 2018-11-20 2020-06-01 海崴生物科技股份有限公司 Continuous plant extraction machine capable of automatically and rapidly extracting plant samples to achieve better extraction rate

Also Published As

Publication number Publication date
TW202206165A (en) 2022-02-16

Similar Documents

Publication Publication Date Title
CN212611389U (en) Supercritical carbon dioxide fluid flash explosion device
CN201285358Y (en) Apparatus for implementing loading under high temperature high pressure environment
TWI739535B (en) High-pressure hydrolysis device and method
WO2015120573A1 (en) Pump-type autoclave system and steam and pressure supply method thereof
CN101477003B (en) Apparatus for loading in high-temperature high-pressure surroundings and its use
CN105347637A (en) Continuous sludge pyrohydrolysis system and method
CN102518577A (en) Vacuum-pumping system for multiple-dewar interlayer and vacuum-pumping method thereof
CN205492445U (en) Super autoclaving device
CN109925748A (en) It is a kind of that the liquid degassing device and method of removing gas liquid can be automatically continuously provided
CN201989324U (en) Defoaming device for pouring resin of composite wind power blade
CN202988999U (en) Novel accelerated carbonation device capable of performing automatic control on humiture, pressure and CO2 concentration
CN109966535B (en) Biological safety type high-pressure sterilizer and sterilization method
CN104891766B (en) Sludge pyrohydrolysis device and method
CN111562188A (en) High-pressure high-flow-rate circulation two-phase flow erosion rate experimental device and experimental method
CN201346461Y (en) Jacketed type grading heating device
CN203737254U (en) Airlift reaction device for producing sugar by hydrolyzing lignocellulose raw materials
CN104342209A (en) Biomass thermal conversion device and use method thereof
CN108485961A (en) The production line of collagen peptide is extracted from wood frog's fallopian tube skin
CN202752020U (en) Device for sugar manufacturing by hydrolyzing of lignocellulose raw materials
CN109529723B (en) Continuous bubbling system in high-temperature and high-pressure kettle
CN208577719U (en) The production line of collagen peptide is extracted from wood frog's fallopian tube skin
CN208014746U (en) It is used to prepare the device of calcium titanium ore bed
WO2021237514A1 (en) Supercritical carbon dioxide fluid flash-explosion machine
CN211372946U (en) Pretreatment device for gas cylinder in production of gas standard substance
CN205868193U (en) Epoxy reation kettle