CN201260906Y - Filter press conveyer device - Google Patents

Filter press conveyer device Download PDF

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Publication number
CN201260906Y
CN201260906Y CNU2008200275536U CN200820027553U CN201260906Y CN 201260906 Y CN201260906 Y CN 201260906Y CN U2008200275536 U CNU2008200275536 U CN U2008200275536U CN 200820027553 U CN200820027553 U CN 200820027553U CN 201260906 Y CN201260906 Y CN 201260906Y
Authority
CN
China
Prior art keywords
filter press
pipeline
utility
model
conveying
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CNU2008200275536U
Other languages
Chinese (zh)
Inventor
李传文
耿德生
沈兴玉
任昌胜
曹长伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong Hualian Mining Co Ltd
Original Assignee
ZIBO HUALIAN MINING CO Ltd
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 ZIBO HUALIAN MINING CO Ltd filed Critical ZIBO HUALIAN MINING CO Ltd
Priority to CNU2008200275536U priority Critical patent/CN201260906Y/en
Application granted granted Critical
Publication of CN201260906Y publication Critical patent/CN201260906Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a filter press conveying device which belongs to the field of press conveying control devices and comprises a filter press connected with a concentrated tank through a pipeline. A conveying pump and a control valve are arranged on the pipeline between the filter press and the concentrated tank. The filter press conveying device is technically characterized in that overpressure return conduits are arranged in parallel on the pipeline between the conveying pump and the control valve, and the other end of each overpressure return conduct is communicated with the concentrated tank. The utility model is improved on the basis of the prior art, the pressure of the pipeline can return in time when exceeding the rated value because the overpressure return conducts are arranged in parallel in the ore solution conveying pipeline, so that the utility model has the advantages of simple structure and convenient implementation, and can guarantee the constant working pressure of the filter press.

Description

The filter press conveying device
Technical field
The utility model belongs to filter press conveying control device field, specifically is a kind of filter press conveying device.
Background technology
The filter press conveying device be barghs such as iron ore must use equipment, with press filtration ore deposit liquid, ore deposit liquid is carried out the processing of subsequent processing, in the production process of enterprise practical, the pressure of filter press always is difficult to constant control, aggravated the working loss of filter press, make the shortening greatly in its service life, produce to such an extent as to influence is normal, and increased bigger production cost to enterprise, for this reason, the pressure under the constant filter press duty how, prolong the service life of filter press, become the technical problem of being badly in need of solution.
The utility model content
The purpose of this utility model is to solve above-mentioned deficiency of the prior art, and prior art is improved, and provides a kind of simple in structure, is convenient to implement, and can ensure the filter press conveying device of the constant operating pressure of filter press.
For achieving the above object, the utility model is achieved through the following technical solutions:
It is a kind of filter press conveying device, comprise the filter press that links by pipeline and concentration basin, delivery pump and by-pass valve control are installed on the pipeline between filter press and the concentration basin, the present technique main points are to be installed in parallel the superpressure return duct, the other end of superpressure return duct and concentration basin UNICOM on the pipeline between delivery pump and the by-pass valve control.
For the ease of further effectively and timely the control valve lineman make pressure under the state, backflow controlled value also is installed on the superpressure return duct.
After the utility model improves prior art, owing in the liquid feed-line of ore deposit, be installed in parallel the superpressure return duct, in time reflux in the time of can making line pressure surpass rating number, therefore have simple in structure, be convenient to implement, can ensure the advantage of the constant operating pressure of filter press.
Description of drawings
Below in conjunction with accompanying drawing the utility model is described in further detail:
Fig. 1: the utility model example structure schematic diagram.
The specific embodiment
As shown in Figure 1, this filter press conveying device, comprise the filter press 7 that links by pipeline 3 and concentration basin 1, delivery pump 2 and by-pass valve control 6 are installed on the pipeline 3 between filter press 7 and the concentration basin 1, the present technique main points are to be installed in parallel superpressure return duct 4, the other end of superpressure return duct 4 and concentration basin 1 UNICOM on the pipeline 3 between delivery pump 2 and the by-pass valve control 6.
For the ease of further effectively and timely the control valve lineman make pressure under the state, backflow controlled value 5 also is installed on superpressure return duct 4.
Like this, during the downforce overrate, ore deposit liquid just is back in the concentration basin 1 by superpressure return duct 4 feed-line timely, immediately feed-line is carried out pressure release, has guaranteed the constant of filter press pressure, has prolonged the service life of filter press 7 in working order.
After the utility model improves prior art, owing in the liquid feed-line of ore deposit, be installed in parallel the superpressure return duct, can Therefore in time reflux when making line pressure surpass rating number, have simple in structurely, be convenient to implement, can ensure that filter press is constant The advantage of operating pressure.

Claims (2)

1, a kind of filter press conveying device, comprise the filter press that links by pipeline and concentration basin, delivery pump and by-pass valve control are installed on the pipeline between filter press and the concentration basin, it is characterized in that being installed in parallel on the pipeline between delivery pump and the by-pass valve control superpressure return duct, the other end of superpressure return duct and concentration basin UNICOM.
2, filter press conveying device according to claim 1 is characterized in that also installing on the superpressure return duct backflow controlled value.
CNU2008200275536U 2008-09-05 2008-09-05 Filter press conveyer device Expired - Fee Related CN201260906Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008200275536U CN201260906Y (en) 2008-09-05 2008-09-05 Filter press conveyer device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008200275536U CN201260906Y (en) 2008-09-05 2008-09-05 Filter press conveyer device

Publications (1)

Publication Number Publication Date
CN201260906Y true CN201260906Y (en) 2009-06-24

Family

ID=40807372

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008200275536U Expired - Fee Related CN201260906Y (en) 2008-09-05 2008-09-05 Filter press conveyer device

Country Status (1)

Country Link
CN (1) CN201260906Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104613317A (en) * 2015-01-16 2015-05-13 江苏华伦化工有限公司 System for preventing liquid in pipeline from expanding
CN105268238A (en) * 2014-06-05 2016-01-27 绍兴拓普斯环保设备有限公司 Stable and low pressure and continuous running filter

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105268238A (en) * 2014-06-05 2016-01-27 绍兴拓普斯环保设备有限公司 Stable and low pressure and continuous running filter
CN104613317A (en) * 2015-01-16 2015-05-13 江苏华伦化工有限公司 System for preventing liquid in pipeline from expanding

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: SHANDONG HUALIAN MINING CO., LTD.

Free format text: FORMER NAME: ZIBO HUALIAN MINING CO., LTD.

CP01 Change in the name or title of a patent holder

Address after: 256119 Zibo County, Shandong City, east of the town of Yiyuan

Patentee after: Shandong Hualian Mining Co., Ltd.

Address before: 256119 Zibo County, Shandong City, east of the town of Yiyuan

Patentee before: Zibo Hualian Mining Co., Ltd.

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20090624

Termination date: 20140905

EXPY Termination of patent right or utility model