CN106731085A - 固液分离机 - Google Patents
固液分离机 Download PDFInfo
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- CN106731085A CN106731085A CN201611161734.3A CN201611161734A CN106731085A CN 106731085 A CN106731085 A CN 106731085A CN 201611161734 A CN201611161734 A CN 201611161734A CN 106731085 A CN106731085 A CN 106731085A
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- 239000007788 liquid Substances 0.000 title claims abstract description 30
- 239000004744 fabric Substances 0.000 claims abstract description 36
- 239000000203 mixture Substances 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 239000007787 solid Substances 0.000 abstract description 9
- 238000000926 separation method Methods 0.000 abstract description 8
- 239000010865 sewage Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 6
- 230000003139 buffering effect Effects 0.000 abstract description 4
- 239000010802 sludge Substances 0.000 abstract description 4
- 239000007921 spray Substances 0.000 abstract description 2
- 235000010469 Glycine max Nutrition 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 239000010828 animal waste Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
- B01D29/03—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/88—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
- B01D29/90—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for feeding
- B01D29/906—Special treatment of the feed stream before contacting the filtering element, e.g. cutting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/88—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
- B01D29/94—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for discharging the filter cake, e.g. chutes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
- B01D29/03—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting
- B01D2029/033—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting bar screens
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Sludge (AREA)
Abstract
本发明公开了一种固液分离机,包括机体、斜置于机体内的筛网,还包括位于机体上部的一段布水槽,以及位于机体下部的一段集泥槽,所述筛网采用条形筛网,由多排沿机体长度方向设置的长条间隔排列组成,本发明设置有布水槽,对所输送进来的污水混合物有一个缓冲的作用,可限制其流速,避免其因压力过大而喷出或流速过快而分离不均,采用的条形筛网,表面不易形成气泡,也就不会阻碍液体流出,集泥槽可及时排出分离后留下的污泥,固液分离效高好。
Description
技术领域
本发明涉及一种固液分离装置,特别适用于对高浓度有机污水的固液分离。
背景技术
目前,固液分离装置可广泛用于各类集约化养殖场对动物粪便的分离,及对酒糟、药渣、淀粉渣、酱渣、屠宰厂等高浓度有机污水的渣液分离,普遍采用的固液分离装置是固液分离机。
现有的固液分离机一般使用穿孔式的筛网,其存在的问题是:当输送泵压力过大时,易导致污水混合物喷出或固液分离不均匀,并且因为液体的张力,容易在筛网孔面形成气泡,阻碍液体的流出,导致分离效果差。
发明内容
本发明旨在至少在一定程度上解决相关技术中的上述技术问题之一。为此,本发明提出一种固液分离机。
本发明解决其技术问题所采用的技术方案是:
固液分离机,包括机体、斜置于机体内的筛网,还包括位于机体上部的一段布水槽,以及位于机体下部的一段集泥槽,所述筛网采用条形筛网,由多排沿机体长度方向设置的长条间隔排列组成。
作为上述技术方案的改进,所述机体底部位于筛网下方的位置设置有出水口。
作为上述技术方案的进一步改进,所述布水槽一个侧面设置有进水口。
进一步,所述集泥槽底部设置有出泥口。
进一步,所述机体左右两侧环绕有高度为10cm的挡水板。
进一步,所述布水槽高出所述挡水板20-30cm。
进一步,所述进水口管底与布水槽底齐平。
本发明的有益效果是:本发明设置有布水槽,对所输送进来的污水混合物有一个缓冲的作用,可限制其流速,避免其因压力过大而喷出或流速过快而分离不均,采用的条形筛网,表面不易形成气泡,也就不会阻碍液体流出,集泥槽可及时排出分离后留下的污泥,本发明固液分离效高好。
附图说明
下面结合附图和实施例对本发明进一步说明。
图1是本发明安装结构示意图。
具体实施方式
参照图1,本发明的固液分离机,包括机体1、斜置于机体1内的筛网2,所述机体1底部位于筛网2下方的位置设置有出水口5,用于排出分离之后的液体,还包括位于机体1上部的一段布水槽3,布水槽3对所输送进来的污水混合物有一个缓冲的作用,可限制其流速,避免其因压力过大而喷出或流速过快而分离不均,所述布水槽3一个侧面设置有进水口6,用于污水混合物的进入,优选的,所述进水口6管底与布水槽3底齐平,以及位于机体1下部的一段集泥槽4,所述集泥槽4底部设置有出泥口7,用于分离后污泥的排出,所述筛网2采用条形筛网,由多排沿机体1长度方向设置的长条间隔排列组成。
所述机体1左右两侧环绕有高度为10cm的挡水板8,所述布水槽3高出所述挡水板8,20-30cm,对污泥混合物具有一定的遮挡作用。
本发明设置有布水槽,对所输送进来的污水混合物有一个缓冲的作用,可限制其流速,避免其因压力过大而喷出或流速过快而分离不均,采用的条形筛网,表面不易形成气泡,也就不会阻碍液体流出,集泥槽可及时排出分离后留下的污泥,本发明固液分离效高好。
以上具体结构和尺寸数据是对本发明的较佳实施例进行了具体说明,但本发明创造并不限于所述实施例,熟悉本领域的技术人员在不违背本发明精神的前提下还可做出种种的等同变形或替换,这些等同的变形或替换均包含在本申请权利要求所限定的范围内。
Claims (7)
1.固液分离机,包括机体(1)、斜置于机体(1)内的筛网(2),其特征在于:还包括位于机体(1)上部的一段布水槽(3),以及位于机体(1)下部的一段集泥槽(4),所述筛网(2)采用条形筛网,由多排沿机体(1)长度方向设置的长条间隔排列组成。
2.根据权利要求1所述的固液分离机,其特征在于:所述机体(1)底部位于筛网(2)下方的位置设置有出水口(5)。
3.根据权利要求1所述的固液分离机,其特征在于:所述布水槽(3)一个侧面设置有进水口(6)。
4.根据权利要求1所述的固液分离机,其特征在于:所述集泥槽(4)底部设置有出泥口(7)。
5.根据权利要求1所述的固液分离机,其特征在于:所述机体(1)左右两侧环绕有高度为10cm的挡水板(8)。
6.根据权利要求5所述的固液分离机,其特征在于:所述布水槽(3)高出所述挡水板(8)20-30cm。
7.根据权利要求3所述的固液分离机,其特征在于:所述进水口(6)管底与布水槽(3)底齐平。
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CN201611161734.3A CN106731085A (zh) | 2016-12-15 | 2016-12-15 | 固液分离机 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110000952A (zh) * | 2019-04-24 | 2019-07-12 | 国家能源投资集团有限责任公司 | 聚烯烃切粒系统及其回收装置 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110000952A (zh) * | 2019-04-24 | 2019-07-12 | 国家能源投资集团有限责任公司 | 聚烯烃切粒系统及其回收装置 |
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