CN106395385A - A diaphragm type pulverized coal pressurized conveying system and conveying method - Google Patents

A diaphragm type pulverized coal pressurized conveying system and conveying method Download PDF

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Publication number
CN106395385A
CN106395385A CN201610994555.1A CN201610994555A CN106395385A CN 106395385 A CN106395385 A CN 106395385A CN 201610994555 A CN201610994555 A CN 201610994555A CN 106395385 A CN106395385 A CN 106395385A
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membrane
space
valve
diaphragm
pulverized coal
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章刚
李宇行
霍耿磊
殷雨田
王卉
刘雪梅
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Changzheng Engineering Co Ltd
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Changzheng Engineering Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/04Conveying materials in bulk pneumatically through pipes or tubes; Air slides
    • B65G53/06Gas pressure systems operating without fluidisation of the materials
    • B65G53/10Gas pressure systems operating without fluidisation of the materials with pneumatic injection of the materials by the propelling gas
    • B65G53/12Gas pressure systems operating without fluidisation of the materials with pneumatic injection of the materials by the propelling gas the gas flow acting directly on the materials in a reservoir
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/34Details
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/34Details
    • B65G53/36Arrangements of containers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/34Details
    • B65G53/58Devices for accelerating or decelerating flow of the materials; Use of pressure generators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G2201/00Indexing codes relating to handling devices, e.g. conveyors, characterised by the type of product or load being conveyed or handled
    • B65G2201/04Bulk

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Reciprocating Pumps (AREA)

Abstract

The invention discloses a diaphragm type pulverized coal pressurized conveying system and a diaphragm type pulverized coal pressurized conveying method, wherein the diaphragm type pulverized coal pressurized conveying system comprises a normal-pressure coal bunker, a high-pressure coal bunker, a first valve, a second valve and a conveying tank, wherein a diaphragm is arranged in the conveying tank, and the conveying tank is provided with a tank body; the diaphragm is provided with two communicating ports which are respectively communicated with the first valve and the second valve and divide the interior of the tank body into an inner membrane space surrounded by the diaphragm and an outer membrane space formed by the diaphragm and the tank body. The diaphragm type pulverized coal pressurized conveying system provided by the invention effectively solves the problems that in the prior art, a large amount of inert gas needs to be discharged, so that the environment pollution is large, the efficiency of the pressurized conveying process is low, continuous adjustability cannot be realized, the high-pressure-resistant equipment needs to be large in size, the manufacturing cost is high, and the like.

Description

一种隔膜式粉煤加压输送系统及输送方法A diaphragm type pulverized coal pressurized conveying system and conveying method

技术领域technical field

本发明涉及粉煤加压输送领域,尤其是一种隔膜式粉煤加压输送系统及输送方法。The invention relates to the field of pulverized coal pressure conveying, in particular to a diaphragm type pulverized coal pressure conveying system and a conveying method.

背景技术Background technique

在煤化工、冶金、食品加工等诸多的领域都涉及到粉体的加压输送过程。煤气化,尤其是粉煤加压气化是一种洁净煤利用技术,在近年来得到快速的发展,进行了越来越广泛的利用。粉煤加压输送技术是粉煤加压气化技术是不可缺少的技术环节。粉煤加压输送技术是将干煤粉从常压提高至某一特定的高压,以实现粉煤在高压下的燃烧与气化。In coal chemical industry, metallurgy, food processing and many other fields, the process of pressurized conveying of powder is involved. Coal gasification, especially pulverized coal pressurized gasification is a clean coal utilization technology, which has been developed rapidly in recent years and has been used more and more widely. Pulverized coal pressurized conveying technology is an indispensable technical link of pulverized coal pressurized gasification technology. Pulverized coal pressurized conveying technology is to increase dry coal powder from normal pressure to a specific high pressure, so as to realize the combustion and gasification of pulverized coal under high pressure.

目前在工业上使用的粉煤加压输送技术主要为锁斗加压输送,其原理是使用高压的惰性气体冲入粉煤加压锁斗,提高压力,与粉煤储罐压力均衡后将粉煤输送至粉煤储罐,使用高压惰性气体置换锁斗中的固体粉煤,然后将粉煤锁斗中的高压惰性气体排放,如此循环。The pulverized coal pressurized conveying technology currently used in industry is mainly lock bucket pressurized conveying. The coal is transported to the pulverized coal storage tank, the solid pulverized coal in the lock hopper is replaced with high-pressure inert gas, and then the high-pressure inert gas in the pulverized coal lock hopper is discharged, and the cycle is like this.

现有技术中存在的技术缺陷有:The technical defect that exists in the prior art has:

1、加压过程需要排放大量的惰性气体如N2、CO2等,造成较大的环境污染;1. The pressurization process needs to discharge a large amount of inert gases such as N2, CO2, etc., causing greater environmental pollution;

2、加压输送过程效率低,不能实现连续可调;2. The efficiency of the pressurized conveying process is low, and continuous adjustment cannot be realized;

3、加压输送需要耐高压设备体积大,造价高。3. Pressurized transportation requires high-pressure resistant equipment with large volume and high cost.

发明内容Contents of the invention

(一)要解决的技术问题(1) Technical problems to be solved

本发明所要解决的技术问题在于如何解决现有技术中需要排放大量惰性气体而造成较大的环境污染,加压输送过程效率低且不能实现连续可调,以及需要耐高压设备体积大造价高等问题。The technical problem to be solved by the present invention is how to solve the problems in the prior art that need to discharge a large amount of inert gas to cause greater environmental pollution, the process of pressurized conveying is inefficient and cannot be continuously adjusted, and the need for high-pressure-resistant equipment is large in volume and high in cost. .

(二)技术方案(2) Technical solution

为了实现上述目的,本发明提供了一种隔膜式粉煤加压输送系统,包括常压煤仓、高压煤仓、第一阀门、第二阀门、输送罐,所述输送罐内设有隔膜,并具有罐体;所述隔膜具有两个连通口,所述连通口分别与所述第一阀门、所述第二阀门连通,并将所述罐体内分隔成由所述隔膜包围成的膜内空间以及由所述隔膜与所述罐体构成的膜外空间。In order to achieve the above object, the present invention provides a diaphragm-type pulverized coal pressurized conveying system, which includes a normal-pressure coal bunker, a high-pressure coal bunker, a first valve, a second valve, and a delivery tank, and a diaphragm is arranged in the delivery tank. And has a tank body; the diaphragm has two communication ports, the communication ports communicate with the first valve and the second valve respectively, and separate the tank body into a membrane surrounded by the diaphragm space and the extramembrane space formed by the diaphragm and the tank body.

优选地,所述膜外空间是密闭的,不与所述第一阀门及所述第二阀门连通。Preferably, the extramembrane space is airtight and does not communicate with the first valve and the second valve.

优选地,所述隔膜具有弹性。Preferably, the membrane is elastic.

优选地,所述膜外空间的体积可随着压力变化而改变,同时所述膜内空间的体积也相应变化。Preferably, the volume of the extra-membrane space can change as the pressure changes, and the volume of the inner-membrane space also changes accordingly.

优选地,所述输送罐具有位于所述罐体上部的液压油入口以及位于所述罐体下部的液压油出口。Preferably, the delivery tank has a hydraulic oil inlet located at the upper part of the tank body and a hydraulic oil outlet located at the lower part of the tank body.

优选地,所述液压油入口及所述液压油出口分别与所述膜外空间连通。Preferably, the hydraulic oil inlet and the hydraulic oil outlet communicate with the outer membrane space respectively.

优选地,还包括液压油缸、液压泵;所述液压油出口、所述液压油缸、所述液压泵及所述液压油入口依次连接。Preferably, a hydraulic oil cylinder and a hydraulic pump are also included; the hydraulic oil outlet, the hydraulic oil cylinder, the hydraulic pump and the hydraulic oil inlet are connected in sequence.

本发明还提供了一种隔膜式粉煤加压输送方法,用于上述隔膜式粉煤加压输送系统,按如下步骤实施:The present invention also provides a diaphragm type pulverized coal pressurized conveying method, which is used in the above diaphragm type pulverized coal pressurized conveying system, and is implemented according to the following steps:

S00:打开所述第一阀门,储存在所述常压煤仓内的粉煤通过重力作用输送至所述输送罐的所述膜内空间中,此时所述膜内空间处于常压状态;S00: Open the first valve, and transport the pulverized coal stored in the normal-pressure coal bunker to the inner membrane space of the delivery tank by gravity, and the inner membrane space is under normal pressure at this time;

S10:关闭所述第一阀门,打开所述第二阀门,所述高压煤仓中的高压气体对所述膜内空间冲压,所述膜内空间中的粉煤在重力作用下进入所述高压煤仓中,此时所述膜内空间中充满高压气体;S10: Close the first valve, open the second valve, the high-pressure gas in the high-pressure coal bunker presses the space inside the membrane, and the pulverized coal in the space inside the membrane enters the high-pressure gas under the action of gravity In the coal bunker, the space inside the membrane is filled with high-pressure gas at this time;

S20:启动所述液压泵,所述液压泵将所述液压油缸中的液压油通过所述液压油入口泵入到所述输送罐的膜外空间中,所述膜外空间体积变大,所述隔膜变形,所述膜内空间随着体积变小将其中大部分高压气体挤压并排入到所述高压煤仓中;S20: Start the hydraulic pump, and the hydraulic pump pumps the hydraulic oil in the hydraulic cylinder into the extra-membrane space of the delivery tank through the hydraulic oil inlet, and the volume of the extra-membrane space becomes larger, so The diaphragm is deformed, and most of the high-pressure gas is squeezed and discharged into the high-pressure coal bunker as the space in the film becomes smaller;

S30:关闭所述第二阀门,并关闭所述液压泵,所述膜内空间的残余高压气体膨胀,将所述膜外空间的液压油通过所述液压油出口压回所述液压油缸中,此时所述膜内空间体积变大,所述隔膜变形,所述膜外空间体积变小;和选择性的S30: closing the second valve and the hydraulic pump, the residual high-pressure gas in the space inside the membrane expands, and presses the hydraulic oil in the space outside the membrane back into the hydraulic cylinder through the hydraulic oil outlet, At this time, the volume of the space inside the membrane becomes larger, the diaphragm deforms, and the volume of the space outside the membrane becomes smaller; and selectively

S40:重复步骤S00-S30,循环往复。S40: Steps S00-S30 are repeated, and the cycle repeats.

当存在步骤S40,系统实现连续操作。When step S40 exists, the system realizes continuous operation.

(二)有益效果(2) Beneficial effects

本发明相比有显著的优点和有益效果:Compared with the present invention, there are significant advantages and beneficial effects:

1.采用设有隔膜并分隔成两个腔的输送罐,通过控制两个腔空间的体积来控制粉煤压力,不需要惰性气体参与输送;1. Use a transport tank with a diaphragm and separate it into two chambers, and control the pulverized coal pressure by controlling the volume of the two chambers, without inert gas participating in the transportation;

2.控制隔膜收缩、膨胀频率、阀门开关频率对加料量进行控制,实现连续调节;2. Control the diaphragm shrinkage, expansion frequency, and valve switching frequency to control the feeding amount and realize continuous adjustment;

3.具有隔膜的输送罐体积小、重量轻,系统所需装置少。3. The transport tank with diaphragm is small in size and light in weight, and the system requires few devices.

附图说明Description of drawings

图1为本发明实施例提供的一种隔膜式粉煤加压输送系统的流程图;Fig. 1 is a flow chart of a diaphragm type pulverized coal pressurized conveying system provided by an embodiment of the present invention;

图2为本发明实施例提供的一种隔膜式粉煤加压输送系统输送罐充液压油前状态示意图;Fig. 2 is a schematic diagram of the state before the hydraulic oil is filled in the delivery tank of a diaphragm type pulverized coal pressurized delivery system provided by the embodiment of the present invention;

图3为本发明实施例提供的一种隔膜式粉煤加压输送系统输送罐充液压油过程中状态示意图;Fig. 3 is a schematic diagram of the state in the process of filling hydraulic oil in the conveying tank of a diaphragm type pulverized coal pressurized conveying system provided by the embodiment of the present invention;

图4为本发明实施例提供的一种隔膜式粉煤加压输送系统输送罐充液压油后状态示意图。Fig. 4 is a schematic diagram of the state of a diaphragm type pulverized coal pressurized conveying system provided by an embodiment of the present invention after the conveying tank is filled with hydraulic oil.

图中:In the picture:

1、常压煤仓;2、液压油缸;3、输送罐;4、高压煤仓;5、液压泵;6、第一阀门;7、第二阀门;3-1液压油入口;3-2液压油出口;3-3罐体;3-4隔膜。1. Atmospheric coal bunker; 2. Hydraulic cylinder; 3. Delivery tank; 4. High pressure coal bunker; 5. Hydraulic pump; 6. First valve; 7. Second valve; 3-1 Hydraulic oil inlet; 3-2 Hydraulic oil outlet; 3-3 tank; 3-4 diaphragm.

具体实施方式detailed description

下面将结合本发明实施例以及附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅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。The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention and the accompanying drawings. Apparently, the described embodiments are only some of the embodiments of the present invention, not all of them. 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

如图1-4所示,本发明提供的一种隔膜式粉煤加压输送系统,包括常压煤仓1、高压煤仓4、第一阀门6、第二阀门7、输送罐3。输送罐3通过第一阀门6与常压煤仓1连通,输送罐3通过第二阀门7与高压煤仓4连通。As shown in Figures 1-4, a diaphragm-type pulverized coal pressurized conveying system provided by the present invention includes an atmospheric coal bunker 1, a high-pressure coal bunker 4, a first valve 6, a second valve 7, and a conveying tank 3. The delivery tank 3 communicates with the normal-pressure coal bunker 1 through the first valve 6 , and the delivery tank 3 communicates with the high-pressure coal bunker 4 through the second valve 7 .

其中,输送罐3内设有隔膜3-4,并具有罐体3-3,隔膜设置在罐体3-3内;隔膜3-4具有两个连通口,连通口分别与第一阀门6、第二阀门7连通,并将罐体3-3内分隔成由隔膜3-4包围成的膜内空间以及由隔膜3-4与罐体3-3构成的膜外空间,膜内空间与膜外空间相互隔离;膜外空间是密闭的,不与第一阀门6及第二阀门7连通;隔膜3-4具有弹性,在膜内空间与膜外空间的压力发生变化时,隔膜3-4能改变形状,膜外空间的体积可随着压力变化而改变,同时膜内空间的体积也相应变化。Wherein, the conveying tank 3 is provided with a diaphragm 3-4, and has a tank body 3-3, and the diaphragm is arranged in the tank body 3-3; the diaphragm 3-4 has two communication ports, and the communication ports are respectively connected to the first valve 6, The second valve 7 communicates and separates the inside of the tank body 3-3 into an intramembrane space surrounded by the diaphragm 3-4 and an extramembrane space formed by the diaphragm 3-4 and the tank body 3-3. The outer space is isolated from each other; the outer space of the membrane is airtight and does not communicate with the first valve 6 and the second valve 7; the diaphragm 3-4 is elastic, and when the pressure of the inner space of the membrane and the outer space of the membrane changes, the diaphragm 3-4 Can change shape, the volume of the space outside the membrane can change with the change of pressure, and the volume of the space inside the membrane also changes accordingly.

具体地,还包括液压油缸2、液压泵4;输送罐3具有位于罐体3-3上部的液压油入口3-1以及位于罐体3-3下部的液压油出口3-2。Specifically, it also includes a hydraulic cylinder 2 and a hydraulic pump 4; the transfer tank 3 has a hydraulic oil inlet 3-1 located at the upper part of the tank body 3-3 and a hydraulic oil outlet 3-2 located at the lower part of the tank body 3-3.

其中,液压油入口3-1及液压油出口3-2分别与膜外空间连通;液压油出口3-2、液压油缸2、液压泵4及液压油入口3-1依次连接,存储在液压油缸2的液压油可以被液压泵4通过液压油入口3-1泵入到输送罐3的膜外空间中,膜外空间中的液压油也能够通过液压油出口3-2压入到液压油缸2中。Among them, the hydraulic oil inlet 3-1 and the hydraulic oil outlet 3-2 are respectively connected with the space outside the membrane; the hydraulic oil outlet 3-2, the hydraulic cylinder 2, the hydraulic pump 4 and the hydraulic oil inlet 3-1 are sequentially connected and stored in the hydraulic cylinder The hydraulic oil in 2 can be pumped into the extra-membrane space of the delivery tank 3 by the hydraulic pump 4 through the hydraulic oil inlet 3-1, and the hydraulic oil in the extra-membrane space can also be pressed into the hydraulic cylinder 2 through the hydraulic oil outlet 3-2 middle.

下面结合本发明实施例中的隔膜式粉煤加压输送系统,详细说明输送系统的输送过程。The conveying process of the conveying system will be described in detail below in conjunction with the diaphragm type pulverized coal pressurized conveying system in the embodiment of the present invention.

打开所述第一阀门6,储存在所述常压煤仓1内的粉煤通过重力作用输送至所述输送罐3的所述膜内空间中,此时所述膜内空间处于常压状态;Open the first valve 6, and the pulverized coal stored in the normal-pressure coal bunker 1 is transported to the membrane inner space of the delivery tank 3 by gravity, and the membrane inner space is at normal pressure ;

关闭所述第一阀门6,打开所述第二阀门7,所述高压煤仓4中的高压气体对所述膜内空间冲压,所述膜内空间中的粉煤在重力作用下进入所述高压煤仓4中,此时所述膜内空间中充满高压气体。Close the first valve 6, open the second valve 7, the high-pressure gas in the high-pressure coal bunker 4 punches the inner space of the membrane, and the pulverized coal in the inner space of the membrane enters the In the high-pressure coal bunker 4, the space in the membrane is filled with high-pressure gas at this time.

启动所述液压泵4,所述液压泵4将所述液压油缸2中的液压油通过所述液压油入口3-1泵入到所述输送罐3的膜外空间中,所述膜外空间体积变大,所述隔膜3-4变形,所述膜内空间随着体积变小将其中大部分高压气体挤压并排入到所述高压煤仓4中。Start the hydraulic pump 4, and the hydraulic pump 4 pumps the hydraulic oil in the hydraulic cylinder 2 into the extra-membrane space of the delivery tank 3 through the hydraulic oil inlet 3-1, and the extra-membrane space As the volume becomes larger, the diaphragm 3-4 is deformed, and most of the high-pressure gas is squeezed and discharged into the high-pressure coal bunker 4 in the space inside the membrane as the volume becomes smaller.

关闭所述第二阀门7,并关闭所述液压泵4,所述膜内空间的残余高压气体膨胀,将所述膜外空间的液压油通过所述液压油出口3-2压回所述液压油缸2中,此时所述膜内空间体积变大,所述隔膜3-4变形,所述膜外空间体积变小。Close the second valve 7, and close the hydraulic pump 4, the residual high-pressure gas in the space inside the membrane expands, and the hydraulic oil in the space outside the membrane is pressed back to the hydraulic pressure through the hydraulic oil outlet 3-2. In the oil cylinder 2, at this time, the volume of the space inside the membrane becomes larger, the diaphragm 3-4 is deformed, and the volume of the space outside the membrane becomes smaller.

重复以上,循环往复。Repeat the above, and the cycle repeats.

实施例2Example 2

如图1所示,本发明提供的一种隔膜式粉煤加压输送方法,步骤如下:As shown in Fig. 1, a kind of membrane type pulverized coal pressure conveying method provided by the present invention, the steps are as follows:

打开所述第一阀门6,储存在所述常压煤仓1内的粉煤通过重力作用输送至所述输送罐3的所述膜内空间中,此时所述膜内空间处于常压状态;Open the first valve 6, and the pulverized coal stored in the normal-pressure coal bunker 1 is transported to the membrane inner space of the delivery tank 3 by gravity, and the membrane inner space is at normal pressure ;

关闭所述第一阀门6,打开所述第二阀门7,所述高压煤仓4中的高压气体对所述膜内空间冲压,所述膜内空间中的粉煤在重力作用下进入所述高压煤仓4中,此时所述膜内空间中充满高压气体;Close the first valve 6, open the second valve 7, the high-pressure gas in the high-pressure coal bunker 4 punches the inner space of the membrane, and the pulverized coal in the inner space of the membrane enters the In the high-pressure coal bunker 4, at this moment, the space in the membrane is filled with high-pressure gas;

启动所述液压泵4,所述液压泵4将所述液压油缸2中的液压油通过所述液压油入口3-1泵入到所述输送罐3的膜外空间中,所述膜外空间体积变大,所述隔膜3-4变形,所述膜内空间随着体积变小将其中大部分高压气体挤压并排入到所述高压煤仓4中;Start the hydraulic pump 4, and the hydraulic pump 4 pumps the hydraulic oil in the hydraulic cylinder 2 into the extra-membrane space of the delivery tank 3 through the hydraulic oil inlet 3-1, and the extra-membrane space When the volume becomes larger, the diaphragm 3-4 is deformed, and most of the high-pressure gas is squeezed and discharged into the high-pressure coal bunker 4 in the space inside the membrane as the volume becomes smaller;

关闭所述第二阀门7,并关闭所述液压泵4,所述膜内空间的残余高压气体膨胀,将所述膜外空间的液压油通过所述液压油出口3-2压回所述液压油缸2中,此时所述膜内空间体积变大,所述隔膜3-4变形,所述膜外空间体积变小;Close the second valve 7, and close the hydraulic pump 4, the residual high-pressure gas in the space inside the membrane expands, and the hydraulic oil in the space outside the membrane is pressed back to the hydraulic pressure through the hydraulic oil outlet 3-2. In the oil cylinder 2, at this time, the volume of the space inside the membrane becomes larger, the diaphragm 3-4 is deformed, and the volume of the space outside the membrane becomes smaller;

重复以上,循环往复。Repeat the above, and the cycle repeats.

整个过程不需要惰性气体参与输送,减少空气污染,通过控制阀门开闭频率,达到对整个输送系统连续控制。The whole process does not require inert gas to participate in the transportation, reducing air pollution, and achieves continuous control of the entire transportation system by controlling the opening and closing frequency of the valve.

以上所述,仅为本发明的一些具体实施方式,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,可轻易想到变化或替换,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应以所述权利要求的保护范围为准。The above are only some specific implementations of the present invention, but the scope of protection of the present invention is not limited thereto. Anyone skilled in the art can easily think of changes or substitutions within the technical scope disclosed in the present invention. All should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention should be determined by the protection scope of the claims.

Claims (8)

1.一种隔膜式粉煤加压输送系统,包括常压煤仓(1)、高压煤仓(4)、第一阀门(6)、第二阀门(7)、输送罐(3),其特征在于:1. A diaphragm type pulverized coal pressurized conveying system comprises a normal pressure coal bunker (1), a high pressure coal bunker (4), a first valve (6), a second valve (7), and a delivery tank (3). Features: 所述输送罐(3)内设有隔膜(3-4),并具有罐体(3-3);The delivery tank (3) is provided with a diaphragm (3-4) and has a tank body (3-3); 所述隔膜(3-4)具有两个连通口,所述连通口分别与所述第一阀门(6)、所述第二阀门(7)连通,并将所述罐体(3-3)内分隔成由所述隔膜(3-4)包围成的膜内空间以及由所述隔膜(3-4)与所述罐体(3-3)构成的膜外空间。The diaphragm (3-4) has two communication ports, the communication ports communicate with the first valve (6) and the second valve (7) respectively, and connect the tank body (3-3) The interior is divided into an inner membrane space surrounded by the membrane (3-4) and an outer membrane space formed by the membrane (3-4) and the tank body (3-3). 2.根据权利要求1所述的隔膜式粉煤加压输送系统,其特征在于:2. The diaphragm type pulverized coal pressurized conveying system according to claim 1, characterized in that: 所述膜外空间是密闭的,不与所述第一阀门(6)及所述第二阀门(7)连通。The extramembrane space is sealed and does not communicate with the first valve (6) and the second valve (7). 3.根据权利要求1所述的隔膜式粉煤加压输送系统,其特征在于:3. The diaphragm type pulverized coal pressurized conveying system according to claim 1, characterized in that: 所述隔膜(3-4)具有弹性。The diaphragm (3-4) has elasticity. 4.根据权利要求1所述的隔膜式粉煤加压输送系统,其特征在于:4. The diaphragm type pulverized coal pressurized conveying system according to claim 1, characterized in that: 所述膜外空间的体积可随着压力变化而改变,同时所述膜内空间的体积也相应变化。The volume of the extramembrane space can change as the pressure changes, and the volume of the intramembrane space also changes accordingly. 5.根据权利要求1所述的隔膜式粉煤加压输送系统,其特征在于:5. The diaphragm type pulverized coal pressurized conveying system according to claim 1, characterized in that: 所述输送罐(3)具有位于所述罐体(3-3)上部的液压油入口(3-1)以及位于所述罐体(3-3)下部的液压油出口(3-2)。The transfer tank (3) has a hydraulic oil inlet (3-1) located at the upper part of the tank body (3-3) and a hydraulic oil outlet (3-2) located at the lower part of the tank body (3-3). 6.根据权利要求5所述的隔膜式粉煤加压输送系统,其特征在于:6. The diaphragm type pulverized coal pressurized conveying system according to claim 5, characterized in that: 所述液压油入口(3-1)及所述液压油出口(3-2)分别与所述膜外空间连通。The hydraulic oil inlet (3-1) and the hydraulic oil outlet (3-2) communicate with the outer membrane space respectively. 7.根据权利要求6所述的隔膜式粉煤加压输送系统,其特征在于:7. The diaphragm type pulverized coal pressurized conveying system according to claim 6, characterized in that: 还包括液压油缸(2)、液压泵(4);It also includes a hydraulic cylinder (2) and a hydraulic pump (4); 所述液压油出口(3-2)、所述液压油缸(2)、所述液压泵(4)及所述液压油入口(3-1)依次连接。The hydraulic oil outlet (3-2), the hydraulic oil cylinder (2), the hydraulic pump (4) and the hydraulic oil inlet (3-1) are connected in sequence. 8.一种隔膜式粉煤加压输送方法,用于权利要求1-7任一项所述的隔膜式粉煤加压输送系统,其特征在于,包括以下步骤:8. A diaphragm type pulverized coal pressurized conveying method for the diaphragm type pulverized coal pressurized conveying system according to any one of claims 1-7, characterized in that it comprises the following steps: S00:打开所述第一阀门(6),储存在所述常压煤仓(1)内的粉煤通过重力作用输送至所述输送罐(3)的所述膜内空间中,此时所述膜内空间处于常压状态;S00: Open the first valve (6), and the pulverized coal stored in the atmospheric coal bunker (1) is transported to the inner membrane space of the delivery tank (3) by gravity. The space inside the membrane is under normal pressure; S10:关闭所述第一阀门(6),打开所述第二阀门(7),所述高压煤仓(4)中的高压气体对所述膜内空间冲压,所述膜内空间中的粉煤在重力作用下进入所述高压煤仓(4)中,此时所述膜内空间中充满高压气体;S10: Close the first valve (6), open the second valve (7), the high-pressure gas in the high-pressure coal bunker (4) punches the space inside the membrane, and the powder in the space inside the membrane Coal enters the high-pressure coal bunker (4) under the action of gravity, and at this time, the space in the membrane is filled with high-pressure gas; S20:启动所述液压泵(4),所述液压泵(4)将所述液压油缸(2)中的液压油通过所述液压油入口(3-1)泵入到所述输送罐(3)的膜外空间中,所述膜外空间体积变大,所述隔膜(3-4)变形,所述膜内空间随着体积变小将其中大部分高压气体挤压并排入到所述高压煤仓(4)中;S20: Start the hydraulic pump (4), and the hydraulic pump (4) pumps the hydraulic oil in the hydraulic cylinder (2) into the delivery tank (3) through the hydraulic oil inlet (3-1) ), the volume of the extramembrane space becomes larger, the diaphragm (3-4) deforms, and the inner space of the membrane squeezes most of the high-pressure gas and discharges it into the high-pressure space as the volume becomes smaller. In the coal bunker (4); S30:关闭所述第二阀门(7),并关闭所述液压泵(4),所述膜内空间的残余高压气体膨胀,将所述膜外空间的液压油通过所述液压油出口(3-2)压回所述液压油缸(2)中,此时所述膜内空间体积变大,所述隔膜(3-4)变形,所述膜外空间体积变小;和选择性的S30: Close the second valve (7), and close the hydraulic pump (4), the residual high-pressure gas in the space inside the membrane expands, and the hydraulic oil in the space outside the membrane passes through the hydraulic oil outlet (3 -2) press back into the hydraulic cylinder (2), at this time the volume of the space inside the membrane becomes larger, the diaphragm (3-4) deforms, and the volume of the space outside the membrane becomes smaller; and optionally S40:重复步骤S00-S30,循环往复。S40: Steps S00-S30 are repeated, and the cycle repeats.
CN201610994555.1A 2016-11-11 2016-11-11 A diaphragm type pulverized coal pressurized conveying system and conveying method Pending CN106395385A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111792382A (en) * 2019-04-09 2020-10-20 航天长征化学工程股份有限公司 Multi-piece plunger type powder pressurized conveying device

Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB854887A (en) * 1957-01-17 1960-11-23 Consolidation Coal Co A pipeline system and controls therefor
GB1146275A (en) * 1966-04-29 1969-03-26 Leipzig Inst Foerdertech Method and apparatus for the pneumatic transportation of powdered and/or granular material
US4604037A (en) * 1984-09-21 1986-08-05 Takesi Hoya Slurry pumping apparatus for solid-liquid separation
DE4131732A1 (en) * 1990-10-22 1992-04-23 Passavant Werke Unit for feeding solid suspension to dewatering device - has storage vessels emptied using compressed air or water which contain deformable membrane
EP0526808A1 (en) * 1991-08-05 1993-02-10 Siemens Aktiengesellschaft Method and device for transporting of powder
US5682929A (en) * 1995-07-21 1997-11-04 Wacker-Chemie Gmbh Method for the filling and emptying of a receptacle
US5746347A (en) * 1995-09-12 1998-05-05 Degussa Aktiengesellschaft Method and apparatus for dispensing particles from a container
US6644930B1 (en) * 1999-04-09 2003-11-11 Oy Pro-Hydro Ab Method and arrangement for pumping a material using a dual chamber pump system
DE10353968A1 (en) * 2003-11-19 2005-07-07 Itw Gema Ag Coating powder conveying device, especially for transporting powder from a storage container, e.g. a sack or bag, has a hose membrane pump for transporting powder that has been fluidized using compressed air
CN2808837Y (en) * 2005-07-11 2006-08-23 西安热工研究院有限公司 Dry pulverized coal pressurized dense-phase conveying device having multiple discharging port
US20090110517A1 (en) * 2007-10-29 2009-04-30 Leon Yuan Catalyst Flow Control Device for Transfer of Solids Between Two Vessels
US20090142148A1 (en) * 2007-11-30 2009-06-04 Leon Yuan Device to Transfer Catalyst from a Low Pressure Vessel to a High Pressure Vessel and purge the Transferred Catalyst
CN102303782A (en) * 2011-09-06 2012-01-04 陕西省煤化工工程技术研究中心 Powder conveying device
WO2012139898A1 (en) * 2011-04-15 2012-10-18 Reinhausen Plasma Gmbh Diaphragm pump and method for delivering fine-grain powder with the aid of a diaphragm pump
CN103303681A (en) * 2013-06-07 2013-09-18 北京神雾环境能源科技集团股份有限公司 Pulverized coal pressure transmission system and process
US20140112802A1 (en) * 2011-04-08 2014-04-24 Frank Hannemann Membrane dust-pumping system
CN204197995U (en) * 2014-09-15 2015-03-11 中天联合节能建设发展(天津)股份有限公司 A kind of diaphragm type powder delivery system
CN105173736A (en) * 2015-10-12 2015-12-23 航天长征化学工程股份有限公司 Powder pressurizing and conveying device, system and method

Patent Citations (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB854887A (en) * 1957-01-17 1960-11-23 Consolidation Coal Co A pipeline system and controls therefor
GB1146275A (en) * 1966-04-29 1969-03-26 Leipzig Inst Foerdertech Method and apparatus for the pneumatic transportation of powdered and/or granular material
US4604037A (en) * 1984-09-21 1986-08-05 Takesi Hoya Slurry pumping apparatus for solid-liquid separation
DE4131732A1 (en) * 1990-10-22 1992-04-23 Passavant Werke Unit for feeding solid suspension to dewatering device - has storage vessels emptied using compressed air or water which contain deformable membrane
EP0526808A1 (en) * 1991-08-05 1993-02-10 Siemens Aktiengesellschaft Method and device for transporting of powder
US5682929A (en) * 1995-07-21 1997-11-04 Wacker-Chemie Gmbh Method for the filling and emptying of a receptacle
US5746347A (en) * 1995-09-12 1998-05-05 Degussa Aktiengesellschaft Method and apparatus for dispensing particles from a container
US6644930B1 (en) * 1999-04-09 2003-11-11 Oy Pro-Hydro Ab Method and arrangement for pumping a material using a dual chamber pump system
DE10353968A1 (en) * 2003-11-19 2005-07-07 Itw Gema Ag Coating powder conveying device, especially for transporting powder from a storage container, e.g. a sack or bag, has a hose membrane pump for transporting powder that has been fluidized using compressed air
CN2808837Y (en) * 2005-07-11 2006-08-23 西安热工研究院有限公司 Dry pulverized coal pressurized dense-phase conveying device having multiple discharging port
US20090110517A1 (en) * 2007-10-29 2009-04-30 Leon Yuan Catalyst Flow Control Device for Transfer of Solids Between Two Vessels
US20090142148A1 (en) * 2007-11-30 2009-06-04 Leon Yuan Device to Transfer Catalyst from a Low Pressure Vessel to a High Pressure Vessel and purge the Transferred Catalyst
US20140112802A1 (en) * 2011-04-08 2014-04-24 Frank Hannemann Membrane dust-pumping system
WO2012139898A1 (en) * 2011-04-15 2012-10-18 Reinhausen Plasma Gmbh Diaphragm pump and method for delivering fine-grain powder with the aid of a diaphragm pump
US20140037466A1 (en) * 2011-04-15 2014-02-06 Reinhausen Plasma Gmbh Diaphragm pump and method for delivering fine-grain powder with the aid of a diaphragm pump
CN102303782A (en) * 2011-09-06 2012-01-04 陕西省煤化工工程技术研究中心 Powder conveying device
CN103303681A (en) * 2013-06-07 2013-09-18 北京神雾环境能源科技集团股份有限公司 Pulverized coal pressure transmission system and process
CN204197995U (en) * 2014-09-15 2015-03-11 中天联合节能建设发展(天津)股份有限公司 A kind of diaphragm type powder delivery system
CN105173736A (en) * 2015-10-12 2015-12-23 航天长征化学工程股份有限公司 Powder pressurizing and conveying device, system and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111792382A (en) * 2019-04-09 2020-10-20 航天长征化学工程股份有限公司 Multi-piece plunger type powder pressurized conveying device
CN111792382B (en) * 2019-04-09 2024-05-28 航天长征化学工程股份有限公司 Multi-piece plunger type powder pressurized conveying device

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Application publication date: 20170215