• ���(y��)
• ���g(sh��)��ˇ
• ��Q����
• ���̰���
• ���͑�(y��ng)��
• ��(zhu��n)�}
• �a(ch��n)Ʒ
• ��I(y��)
• ���߷�Ҏ(gu��)
• ��(bi��o)��(zh��n)Ҏ(gu��)��
• ��„
• ֪�R(sh��)��
• �̘I(y��)�C(j��)��(hu��)
• ��(hu��)�hչ�[

����-������ˇ̎���켈�Uˮ���̌�(sh��)�����坍���a(ch��n)

ժҪ: ��B���f(w��n)¡�켈�S�Uˮ̎�����̸Ľ���(sh��)��,�������˅��� ������ˇ���ԭ������ˇ�ă�(y��u)��(sh��)�����\(y��n)�Р�r�c̎���ɱ�,�����̸��첢��(sh��)���坍���a(ch��n)����Ⱦ���|(zh��)�ŷſ������@�p��,��ˮ�|(zh��)���_(d��)��GB18918-2002һ��(j��)A��(bi��o)��(zh��n),���M��һ�����ˮ���|(zh��)��Ҫ��ͬ�r(sh��)�cԭ�еĺ�������̎����ˇ��ȿɹ�(ji��)ʡ��(d��ng)���s55%,�����̲�ȡ��(ji��)ˮ��ʩ��,���a(ch��n)Ʒ��ˮ��?j��)H��7��9 m3/t����Ч������ˮ�YԴ����,��ͨ�^(gu��)�\(y��n)�Р�r��֪�������෨���酒����̎����ˇ�������Ʒ���,���������^���ܽ�����0.9��1.2 mg/L���l�����\(y��n)�У���Ч�p�����ܺ�,���nj�(sh��)�H�������^������ą�����̎����ˇ,��

����ժҪ:

��B���f(w��n)¡�켈�S�Uˮ̎�����̸Ľ���(sh��)���������˅��� ������ˇ���ԭ������ˇ�ă�(y��u)��(sh��)�����\(y��n)�Р�r�c̎���ɱ�,�����̸��첢��(sh��)���坍���a(ch��n)��,����Ⱦ���|(zh��)�ŷſ������@�p�٣�ˮ�|(zh��)���_(d��)��GB18918-2002һ��(j��)A��(bi��o)��(zh��n),���M��һ�����ˮ���|(zh��)��Ҫ��,��ͬ�r(sh��)�cԭ�еĺ�������̎����ˇ��ȿɹ�(ji��)ʡ��(d��ng)���s55%�����̲�ȡ��(ji��)ˮ��ʩ��,���a(ch��n)Ʒ��ˮ��?j��)H��7��9 m3/t,����Ч������ˮ�YԴ���ġ�ͨ�^(gu��)�\(y��n)�Р�r��֪�������෨���酒����̎����ˇ�������Ʒ���,���������^���ܽ�����0.9��1.2 mg/L���l�����\(y��n)��,����Ч�p�����ܺģ��nj�(sh��)�H�������^������ą�����̎����ˇ,��

Ӣ��ժҪ:

The wastewater treatment reconstruction project in Wanlong Paper Mill was introduced. The operational process and treament costs were compared�� it could be concluded that anaerobic-aerobic process was more advantaged than the former aerobic treatment process. After the reconstruction of the project and clean production accomplished,�� the effluent quality could achieve first grade discharge standard of GB 18918-2002 and the recycle requirement of reuse water. Meanwhile,�� the energy costs of the new process were reduced by 55%�� comparing with the former aerobic biological treatment technology. With the water conservation technology,�� the water comsumption for per unity unit product was just 7��9 m3/t,�� protecting the water resource effectively. The result indicated that as a developed post-treatment process,�� the activated sludge system was convenient to be operated�� while the dissolved oxygen concentration was low (0.9��1.2 mg/L),�� it presents an attractive characteristic of low energy consumption.

•�����D(zhu��n)�d�����dz��ڂ��f������Ϣ֮Ŀ��,�����Ё�(l��i)Դ��(bi��o)ע�e(cu��)�`���ַ������ĺϷ���(qu��n)�棬Ո(q��ng)���߳֙�(qu��n)���C���c���W(w��ng)“(li��n)ϵ,���҂������r(sh��)����,���h�����x�x,��

  ʹ��΢��“��һ��”��������“���v�h(hu��n)���W(w��ng)”

�����Ҫ�˽����Ԕ��(x��)�ă�(n��i)��,��Ո(q��ng)�c(di��n)�����d 201407151554438197.zip 
        ���dԓ����Ո(q��ng)��������߀���DZ��W(w��ng)��(hu��)�T,��Ո(q��ng)��ע��(c��)